JP2006257237A - Mastication method of natural rubber - Google Patents

Mastication method of natural rubber Download PDF

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JP2006257237A
JP2006257237A JP2005075742A JP2005075742A JP2006257237A JP 2006257237 A JP2006257237 A JP 2006257237A JP 2005075742 A JP2005075742 A JP 2005075742A JP 2005075742 A JP2005075742 A JP 2005075742A JP 2006257237 A JP2006257237 A JP 2006257237A
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natural rubber
mastication
odor
rubber
mass
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Hideki Aoyama
秀樹 青山
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Bridgestone Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a mastication method of a natural rubber which simply and effectively reduces the odor generated on the mastication of the natural rubber irrespective of the kind of the natural rubber. <P>SOLUTION: In the mastication method of a natural rubber in a Banbury mixer, the temperature for allowing the natural rubber to fall from the Banbury mixer to be taken out is set at ≤145°C. Preferably, zinc white and/or carbon black is added to the natural rubber in an amount of ≤5 pts.mass based on 100 pts.mass natural rubber on the mastication. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、天然ゴムの素練り方法に関し、詳しくは天然ゴムの素練り中に発生する天然ゴム特有の臭気を低減し得る天然ゴムの素練り方法に関する。   The present invention relates to a method for masticating natural rubber, and more particularly to a method for masticating natural rubber that can reduce the odor peculiar to natural rubber generated during mastication of natural rubber.

一般的に、ゴム業界で用いられている天然ゴムは、熱帯地方に栽培されるヘベア・ブラジリエンスと呼ばれるゴムの樹の樹液(天然ゴムラテックス)を凝固・乾燥して得られるものである。この天然ゴムを製造する方法には、その製法により、主として技術的各付けゴム(TSR;TECHNICALLY SPECIFIED RUBBER)と薫製ゴム(RSS;RIBBED SMOKED SHEET)に大別されている。   In general, the natural rubber used in the rubber industry is obtained by coagulating and drying a sap of a rubber tree (natural rubber latex) called Hevea brasiliens cultivated in the tropics. The methods for producing this natural rubber are roughly classified into technical rubbers (TSR) and technical rubber (RSS).

TSRは、上級グレードと下級グレードに分類されている。上級グレードTSRは、新鮮なラテックスを酸で凝固し、それを水洗・粉砕し、更に120℃前後の熱風で乾燥して製造される。また、下級グレードTSRは、ゴムの樹のラテックス回収カップ内でラテックスが自然凝固してできたカップランプや、小規模農家が採取したラテックスを自然凝固させて得られるスラブ等を水洗・粉砕し、更に乾燥して製造される。これに対して、RSSは、ラテックスを酸で凝固し、ロールでシート状に圧延して未薫製シート(USS)を作り、更にこれを薫製して得られる。   TSR is classified into advanced grade and lower grade. The high grade TSR is produced by coagulating fresh latex with acid, washing and pulverizing it with water, and drying it with hot air at around 120 ° C. In addition, the lower grade TSR washes and pulverizes cup lamps made by natural coagulation of latex in latex recovery cups of rubber trees, and slabs obtained by natural coagulation of latex collected by small-scale farmers. Further, it is manufactured by drying. On the other hand, RSS is obtained by coagulating latex with an acid, rolling it into a sheet form with a roll to make an unmade sheet (USS), and further smoking it.

これらの製法により製造された天然ゴムは、出荷前にポリエチレンで梱包されたり、タルクで表面をコーティングされたりすることにより、あるいはゴムの温度が既に室温まで下がっていることにより、流通時点では臭気は小さくて問題にならないものである。   The natural rubber produced by these manufacturing methods is packed with polyethylene before shipment, coated with talc, or because the temperature of the rubber has already dropped to room temperature. It is small and does not cause a problem.

ところで、一般的に、天然ゴムは、合成ゴムと比較して分子量が大きいため、ゴム製品工場において各種配合剤を均一に混練りすることが難しいことから、天然ゴムを少量の素練り促進剤と共に混練りし、ゴム分子量を適度な大きさに下げる操作が必要となる。この操作を、「素練り」という。   By the way, in general, natural rubber has a higher molecular weight than synthetic rubber, so it is difficult to uniformly knead various compounding agents in a rubber product factory. The operation of kneading and lowering the rubber molecular weight to an appropriate size is required. This operation is called “scouring”.

素練りする場合、練りが促進されるに伴って熱が発生し、練られているゴム配合物の温度が上昇する。この温度の上昇に伴って生じるゴム焼け等の問題を回避する目的で、通常、天然ゴムをバンバリーミキサに投入した後、しゃく解剤(素練り促進剤)をゴム分100質量部に対し0.1質量部以下の範囲で添加して約150〜180℃で練っている。   When kneading, heat is generated as the kneading is promoted, and the temperature of the kneaded rubber compound rises. For the purpose of avoiding problems such as rubber burning caused by the increase in temperature, natural rubber is usually added to a Banbury mixer, and then a peptizer (peptizer) is added in an amount of 0. It is added in the range of 1 part by mass or less and kneaded at about 150 to 180 ° C.

しかし、バンバリーミキサ自体の冷却効率だけでは、天然ゴムの混練物の温度上昇を十分に抑えることができないため、通常では、1〜3分でバンバリーミキサからアンダーロールへ落下させ、取り出す工程を複数回繰り返して多ステージとすることが一般的である。   However, since the temperature rise of the natural rubber kneaded product cannot be sufficiently suppressed only by the cooling efficiency of the Banbury mixer itself, usually, the process of dropping from the Banbury mixer to the under roll in one to three minutes and taking it out is performed several times. It is common to repeat the process in multiple stages.

このような素練り工程中に、従来、天然ゴムに含有されていた臭気成分が発散されると共に、非ゴム成分が更に酸化・分解し新たな臭気が発散されていた。これらの臭気が工場内外に漏れると環境問題に発展するおそれがある。   During such a mastication process, odor components conventionally contained in natural rubber are emitted, and non-rubber components are further oxidized and decomposed to emit new odors. If these odors leak into and out of the factory, they may develop into environmental problems.

天然ゴムの素練りにより発生する臭気を補足してGC−MSで分析すると、酢酸やプロピオン酸などの低級脂肪酸類、アルデヒド類、プラジン類やピロール類等の窒素環状化合物、アンモニア等が検出されることが知られている。   When the odor generated by mastication of natural rubber is supplemented and analyzed by GC-MS, lower fatty acids such as acetic acid and propionic acid, aldehydes, nitrogen cyclic compounds such as prazines and pyrroles, ammonia, etc. are detected. It is known.

この臭気問題の対策のため、これまでに、素練り設備の排気ダクトに脱臭フィルターを設置したり、素練り設備周辺に香料を散布したり、様々な対応策を講じてきたが、それでも、対策が充分でない場合があり、更に、天然ゴムそのものの改善、すなわち、天然ゴムの臭気を低減する方法として、例えば、天然ラテックスからの天然ゴムを製造するに際し、天然ゴムラテックスを凝固前または凝固後に水酸化ナトリウム、水酸化カリウム、水酸化カルシウムから選ばれる1種以上のアルカリ溶液に接触させることにより、微生物によって非ゴム分から作り出される臭気成分の揮発性脂肪酸を不揮発性の脂肪酸に変えることにより臭いを低減した天然ゴムの製造方法が知られている(特許文献1)。   To combat this odor problem, various countermeasures have been taken so far, such as installing a deodorizing filter in the exhaust duct of the kneading equipment or spraying fragrance around the kneading equipment. Further, as a method for improving the natural rubber itself, that is, for reducing the odor of the natural rubber, for example, when producing natural rubber from natural latex, By contacting with one or more alkaline solutions selected from sodium oxide, potassium hydroxide, and calcium hydroxide, odors are reduced by changing volatile fatty acids, which are odorous components produced from non-rubber components by microorganisms, to non-volatile fatty acids. A natural rubber production method is known (Patent Document 1).

また、天然ゴムの生産工程において、凝固前のラテックスに特定の臭気低減成分を乾燥ゴム分100質量部に対して、特定量の範囲で添加することにより、天然ゴムに含まれる揮発性脂肪酸のみならず、アルデヒド類、窒素環状化合物、アンモニアなどの分解などによる特有の臭気成分の生成を抑制せしめて、臭気をより効果的に低減し得ることが知られている(特許文献2)。
特開平8−81504号公報(特許請求の範囲等) 特開2005−29590号公報(特許請求の範囲等)
Further, in the natural rubber production process, by adding a specific odor reducing component to the latex before coagulation in a specific amount range with respect to 100 parts by mass of dry rubber, only volatile fatty acids contained in natural rubber can be obtained. In addition, it is known that odors can be more effectively reduced by suppressing generation of unique odor components due to decomposition of aldehydes, nitrogen cyclic compounds, ammonia, and the like (Patent Document 2).
JP-A-8-81504 (claims, etc.) Japanese Patent Laying-Open No. 2005-29590 (Claims etc.)

しかしながら、上記特許文献1に記載される技術は、微生物によって非ゴム分から作り出される臭気成分の揮発性脂肪酸を不揮発性の脂肪酸に変えることにより臭いを低減するものであるが、天然ゴムの臭気成分は揮発性脂肪酸のみならず、アルデヒド類、窒素環状化合物、アンモニアなど多く存在するものであり、この技術では未だ天然ゴムの臭気を満足できる程度に低減するには至っていない。   However, the technique described in Patent Document 1 is to reduce the odor by changing the volatile fatty acid of the odor component produced from the non-rubber component by microorganisms to a non-volatile fatty acid, but the odor component of natural rubber is Not only volatile fatty acids but also aldehydes, nitrogen cyclic compounds, ammonia and the like are present, and this technology has not yet reduced the odor of natural rubber to a satisfactory level.

また、上記特許文献2に記載される技術は、凝固前のラテックスに特定の臭気低減成分を特定量の範囲で添加することが必要であり、従来の手法で製造された通常の天然ゴムには適用することができなかった。   In addition, the technique described in Patent Document 2 requires that a specific odor reducing component is added to the latex before coagulation in a specific amount range. Could not be applied.

そこで本発明の目的は、上記問題点を解消し、天然ゴムの素練り時に発生する臭気を天然ゴムの種類に関係なく簡便かつ効果的に低減し得る天然ゴムの素練り方法を提供することにある。   Accordingly, an object of the present invention is to provide a natural rubber mastication method that can easily and effectively reduce the odor generated during mastication of natural rubber regardless of the type of natural rubber, eliminating the above problems. is there.

本発明者らは、上記課題を解決すべく鋭意検討した結果、天然ゴムをバンバリーミキサにて素練りする際の取り出し温度を所定の温度以下とすることにより上記目的を達成し得ることを見出し、本発明を完成するに至った。   As a result of intensive studies to solve the above problems, the present inventors have found that the above object can be achieved by setting the extraction temperature when masticating natural rubber with a Banbury mixer to a predetermined temperature or lower, The present invention has been completed.

即ち、本発明の天然ゴムの素練り方法は、天然ゴムをバンバリーミキサにて素練りする天然ゴムの素練り方法において、前記天然ゴムを前記バンバリーミキサから落下させ、取り出すときの該天然ゴムの温度を145℃以下とすることを特徴とするものである。   That is, the natural rubber mastication method of the present invention is a natural rubber mastication method in which natural rubber is masticated by a Banbury mixer, and the natural rubber is dropped from the Banbury mixer and taken out. Is 145 ° C. or lower.

本発明においては、素練りの時に前記天然ゴムに亜鉛華を添加することが好ましく、より好ましくは前記天然ゴム100質量部に対し5質量部以下で添加する。また、素練り時に前記天然ゴムにカーボンブラックを添加することも好ましく、より好ましくは前記天然ゴム100質量部に対し5質量部以下で添加する。   In the present invention, it is preferable to add zinc white to the natural rubber during mastication, more preferably 5 parts by mass or less with respect to 100 parts by mass of the natural rubber. Moreover, it is also preferable to add carbon black to the natural rubber during mastication, more preferably 5 parts by mass or less with respect to 100 parts by mass of the natural rubber.

本発明によれば、天然ゴムの素練り時に発生する臭気を天然ゴムの種類に関係なく簡便かつ効果的に低減することができる。   ADVANTAGE OF THE INVENTION According to this invention, the odor which generate | occur | produces at the time of mastication of natural rubber can be reduced simply and effectively irrespective of the kind of natural rubber.

以下、本発明の実施の形態につき具体的に説明する。
本発明においては、天然ゴムの素練り物をバンバリーミキサからアンダーロールへ落下させる際の温度を145℃以下とすることは肝要である。本発明者は鋭意実験を重ねた結果、この温度が149℃を超えると急激に臭気が強くなることを見出し(図1参照)、さらに検討を重ねた結果、落下温度のバラツキを考慮すると、大幅な臭気低減には145℃以下まで規制することが必要であることが分かった。また、このことは、実験室におけるDSCによる天然ゴムの加熱減量も150℃付近より急激に重量が減って揮発物が大幅に発生していることからも理解することができる(図2参照)。即ち、図1から、素練りの臭気は、落下温度が145〜150℃のときに変曲点があり、このとき天然ゴム種の差は小さいことが分かる。また、図1に示すグラフの曲線は、図2に示すDSCの分析による加熱減量曲線と類似しており、このことからも、落下温度を規制することで臭気を低減することができることが分かる。
Hereinafter, embodiments of the present invention will be specifically described.
In the present invention, it is important to set the temperature when the natural rubber paste is dropped from the Banbury mixer to the under roll to 145 ° C. or lower. As a result of repeated experiments, the present inventor has found that the odor suddenly increases when this temperature exceeds 149 ° C. (see FIG. 1). It has been found that it is necessary to regulate the temperature to 145 ° C. or lower for proper odor reduction. This can also be understood from the fact that the loss of heat of natural rubber by DSC in the laboratory is drastically reduced from around 150 ° C. and volatiles are greatly generated (see FIG. 2). That is, it can be seen from FIG. 1 that the odor of mastication has an inflection point when the drop temperature is 145 to 150 ° C., and the difference between the natural rubber types is small at this time. Moreover, the curve of the graph shown in FIG. 1 is similar to the heating loss curve by the DSC analysis shown in FIG. 2, and this also shows that the odor can be reduced by regulating the drop temperature.

本発明において使用し得るバンバリーミキサの諸条件は、上記落下温度以外は従来の素練り工程で採用していた条件をそのまま採用することができ、例えば、バンバリーミキサのロータ部分の容積を除いた実質対比の充填率を表すフィルファクタを50〜80%、ロータの回転数を8〜80rpmなどとすることができる。   The conditions of the Banbury mixer that can be used in the present invention can be the same as those employed in the conventional mastication process except for the above-mentioned drop temperature. For example, the conditions except for the volume of the rotor part of the Banbury mixer can be used. The fill factor representing the contrast filling rate can be set to 50 to 80%, and the rotational speed of the rotor can be set to 8 to 80 rpm.

また、本発明においては、臭気低減の観点から、素練り時に天然ゴムに亜鉛華とカーボンブラックとを同時に、あるいはいずれか一方を添加することが好ましく、より好ましくはこれらを天然ゴム100質量部に対し5質量部以下で添加する。5質量部を超えて添加することは、その後の混練りに悪影響を及ぼすため、好ましくない。   In the present invention, from the viewpoint of reducing odor, it is preferable to add zinc oxide and carbon black to the natural rubber at the same time, or more, at the time of mastication, and more preferably to 100 parts by mass of the natural rubber. However, it is added at 5 parts by mass or less. It is not preferable to add more than 5 parts by mass because it adversely affects the subsequent kneading.

さらに、本発明においては、天然ゴムに、通常、しゃく解剤(素練り促進剤)として使用されているチオフェノールやジスルフィド等を適宜添加することができる。   Furthermore, in the present invention, thiophenol, disulfide, and the like that are usually used as a peptizer (peptizer) can be appropriately added to natural rubber.

次に、本発明を実施例及び比較例に基づいて具体的かつ詳細に説明する。
〔実施例1〜3及び比較例1,2〕
下記表1に示す配合処方、およびバンバリーミキサからの素練り物の落下時温度に従い、天然ゴムをバンバリーミキサで素練りした。この素練り時の臭気濃度を下記に従い評価した。これらの結果を図3に示す。
Next, the present invention will be described specifically and in detail based on examples and comparative examples.
[Examples 1 to 3 and Comparative Examples 1 and 2]
Natural rubber was masticated with a Banbury mixer according to the formulation shown in Table 1 below and the temperature at which the masticated material dropped from the Banbury mixer. The odor concentration during mastication was evaluated according to the following. These results are shown in FIG.

臭気濃度の評価は、以下のような手順1)〜6)で実施した。
1)試験室用の3.7リッターのバンバリーミキサーで、循環水70℃、ローター回転数70rpmの条件で、3分30秒間素練りした。
2)素練り後、直ちにラムを上昇させ、ゴム投入口から排出する臭気の混じった空気をポンプでサンプリングバックに約2分間、約5リッター回収した。
3)サンプリングバッグに回収された臭気の混じった空気を、化学用シリンジで規定量採取し、それを予め清浄な空気を満たしておいた3リッターの臭い袋に注入した(サンプル)。注入量mlと3リッターとで希釈倍率を求めておく。例えば、注入量が1mlであれば、希釈倍率は3000である。
4)少なくとも3名の臭気モニターによって、清浄な空気と比較してサンプルに臭いが感じられるかどうかを鼻で臭いを判定した。
5)臭いが感じられるなら、希釈倍率を上げたサンプルを準備し、再度モニターによって臭いが感じられるかどうかを判定した。
6)臭いが感じられなくなった希釈倍率を臭気濃度とした。
The odor concentration was evaluated by the following procedures 1) to 6).
1) Using a 3.7 liter Banbury mixer for a test room, mastication was performed for 3 minutes and 30 seconds under conditions of circulating water at 70 ° C. and a rotor rotation speed of 70 rpm.
2) Immediately after mastication, the ram was raised immediately, and the odor mixed air discharged from the rubber inlet was collected for about 2 liters for about 2 minutes in a sampling back with a pump.
3) A prescribed amount of odor mixed air collected in the sampling bag was sampled with a chemical syringe and injected into a 3 liter odor bag filled with clean air in advance (sample). The dilution rate is determined with an injection volume of ml and 3 liters. For example, if the injection volume is 1 ml, the dilution factor is 3000.
4) The odor was judged by the nose with an odor monitor of at least 3 people to see if the sample felt odor compared to clean air.
5) If a smell was felt, a sample with an increased dilution factor was prepared, and it was judged again whether or not the smell was felt by a monitor.
6) The dilution ratio at which no odor was felt was taken as the odor concentration.

Figure 2006257237
1)ノクタイザーSK(大内新興化学工業(株)製)
2)RSS:RIBBED SMOKED SHEET(品番:RSS#4)
3)TSR:TECHNICALLY SPECIFIED RUBBER(品番:SMR#20)
4)TSR:TECHNICALLY SPECIFIED RUBBER(品番:SIR#20)
Figure 2006257237
1) Noctizer SK (Ouchi Shinsei Chemical Co., Ltd.)
2) RSS: RIBBED SMOKED SHEEET (Part No .: RSS # 4)
3) TSR: TECHNICALLY SPECIFED RUBBER (Part No .: SMR # 20)
4) TSR: TECHNICALLY SPECIFED RUBBER (Part No .: SIR # 20)

表1および図3から、天然ゴムの種類に関係なく、素練りの落下温度を145℃以下に規制することで臭気を低減することができることが分かる。また、亜鉛華とカ−ボンを併用することで更なる効果が得られることも分かる。   It can be seen from Table 1 and FIG. 3 that the odor can be reduced by regulating the kneading drop temperature to 145 ° C. or lower regardless of the type of natural rubber. Moreover, it turns out that the further effect is acquired by using together zinc white and carbon.

RSSおよびTSRの落下温度と臭気濃度との関係を示すグラフである。It is a graph which shows the relationship between the fall temperature of RSS and TSR, and an odor density | concentration. 落下温度と減量速度との関係を示すグラフである。It is a graph which shows the relationship between drop temperature and weight loss rate. 実施例1〜3および比較例1、2における落下温度と臭気温度との関係を表すグラフである。It is a graph showing the relationship between the fall temperature and odor temperature in Examples 1-3 and Comparative Examples 1,2.

Claims (5)

天然ゴムをバンバリーミキサにて素練りする天然ゴムの素練り方法において、前記天然ゴムを前記バンバリーミキサから落下させ、取り出すときの該天然ゴムの温度を145℃以下とすることを特徴とする天然ゴムの素練り方法。   In a natural rubber mastication method in which natural rubber is masticated with a Banbury mixer, the natural rubber is dropped from the Banbury mixer and the temperature of the natural rubber when taken out is 145 ° C. or less. The method of practicing. 素練り時に前記天然ゴムに亜鉛華を添加する請求項1記載の素練り方法。   The mastication method according to claim 1, wherein zinc white is added to the natural rubber during mastication. 前記亜鉛華を前記天然ゴム100質量部に対し5質量部以下で添加する請求項2記載の素練り方法。   The mastication method according to claim 2, wherein the zinc white is added at 5 parts by mass or less with respect to 100 parts by mass of the natural rubber. 素練りの時に前記天然ゴムにカーボンブラックを添加する請求項1〜3のうちいずれか一項記載の素練り方法。   The mastication method according to any one of claims 1 to 3, wherein carbon black is added to the natural rubber during mastication. 前記カーボンブラックを前記天然ゴム100質量部に対し5質量部以下で添加する請求項4記載の素練り方法。   The mastication method according to claim 4, wherein the carbon black is added at 5 parts by mass or less with respect to 100 parts by mass of the natural rubber.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008144080A (en) * 2006-12-12 2008-06-26 Bridgestone Corp Method for masticating natural rubber
JP2008143972A (en) * 2006-12-07 2008-06-26 Toyo Tire & Rubber Co Ltd Manufacturing method for natural rubber composition, natural rubber composition and pneumatic tire

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0881504A (en) * 1994-09-14 1996-03-26 Yokohama Rubber Co Ltd:The Production of natural rubber
JPH08302069A (en) * 1995-05-01 1996-11-19 Bridgestone Corp Deodorizing agent for natural rubber, deodorized natural rubber composition and its production
JPH11222502A (en) * 1998-02-06 1999-08-17 Bando Chem Ind Ltd Method for masticating natural rubber
JP2002138102A (en) * 2000-11-02 2002-05-14 Bridgestone Corp Method of producing tsr-type natural rubber
JP2005029590A (en) * 2003-07-07 2005-02-03 Bridgestone Corp Natural rubber with reduced odor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0881504A (en) * 1994-09-14 1996-03-26 Yokohama Rubber Co Ltd:The Production of natural rubber
JPH08302069A (en) * 1995-05-01 1996-11-19 Bridgestone Corp Deodorizing agent for natural rubber, deodorized natural rubber composition and its production
JPH11222502A (en) * 1998-02-06 1999-08-17 Bando Chem Ind Ltd Method for masticating natural rubber
JP2002138102A (en) * 2000-11-02 2002-05-14 Bridgestone Corp Method of producing tsr-type natural rubber
JP2005029590A (en) * 2003-07-07 2005-02-03 Bridgestone Corp Natural rubber with reduced odor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008143972A (en) * 2006-12-07 2008-06-26 Toyo Tire & Rubber Co Ltd Manufacturing method for natural rubber composition, natural rubber composition and pneumatic tire
JP2008144080A (en) * 2006-12-12 2008-06-26 Bridgestone Corp Method for masticating natural rubber

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