JPS5914401B2 - Method for manufacturing molded sulfur - Google Patents
Method for manufacturing molded sulfurInfo
- Publication number
- JPS5914401B2 JPS5914401B2 JP8059075A JP8059075A JPS5914401B2 JP S5914401 B2 JPS5914401 B2 JP S5914401B2 JP 8059075 A JP8059075 A JP 8059075A JP 8059075 A JP8059075 A JP 8059075A JP S5914401 B2 JPS5914401 B2 JP S5914401B2
- Authority
- JP
- Japan
- Prior art keywords
- sulfur
- rubber
- present
- wax
- molded
- 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
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims description 61
- 239000011593 sulfur Substances 0.000 title claims description 61
- 229910052717 sulfur Inorganic materials 0.000 title claims description 61
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 238000000034 method Methods 0.000 title description 8
- 238000002844 melting Methods 0.000 claims description 8
- 230000008018 melting Effects 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 238000000465 moulding Methods 0.000 claims description 2
- 229920001971 elastomer Polymers 0.000 description 18
- 239000005060 rubber Substances 0.000 description 18
- 239000001993 wax Substances 0.000 description 12
- 239000007788 liquid Substances 0.000 description 8
- 239000000428 dust Substances 0.000 description 7
- 238000004073 vulcanization Methods 0.000 description 6
- 238000004880 explosion Methods 0.000 description 5
- 239000004200 microcrystalline wax Substances 0.000 description 5
- 235000019808 microcrystalline wax Nutrition 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 238000010298 pulverizing process Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000010058 rubber compounding Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 229920003052 natural elastomer Polymers 0.000 description 2
- 229920001194 natural rubber Polymers 0.000 description 2
- 239000004636 vulcanized rubber Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 229920000459 Nitrile rubber Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000012164 animal wax Substances 0.000 description 1
- 229920005549 butyl rubber Polymers 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229920003244 diene elastomer Polymers 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- -1 for example Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012184 mineral wax Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010057 rubber processing Methods 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
- 235000014692 zinc oxide Nutrition 0.000 description 1
Landscapes
- Processes Of Treating Macromolecular Substances (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】
本発明は、ゴム配合剤として有用な分散性にすぐれた成
型イオウの製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing molded sulfur having excellent dispersibility and useful as a rubber compounding agent.
イオウはゴム配合剤として、ジエン系ゴム、すなわち天
然ゴムあるいはスチレンブタジエンゴムアクリロニトリ
ルブタジエンゴム、イソプレンゴム、ブタジエンゴム、
ブチルゴムなどの合成ゴムの加硫において、促進剤およ
び亜鉛華と共に、本質的に加硫反応に関与する最も大切
な物質である。しかしながら、イオウが粗粒子のまま、
加硫すべきゴム中に存在すると、加硫に際して、粗粒子
の存在する部分は局部的に過加硫となり、加硫後はこの
部分の後改硫が進行して、ゴム製品の老化5 が早くな
る。したがつて、イオウはできるだけ微粒子であること
が望ましく、現在普通ドライ・ラバー用のイオウとして
は、200〜300メッシュ以上の微粉末のものが用い
られている。今日、粉末イオウを工業的に製造する最も
普通70の方法は、塊状イオウを粉砕機によつて粉末に
し、これを分級して一定粒度の部分を採取する方法であ
る。Sulfur is used as a rubber compounding agent in diene rubbers, namely natural rubber or styrene-butadiene rubber, acrylonitrile-butadiene rubber, isoprene rubber, butadiene rubber,
In the vulcanization of synthetic rubbers such as butyl rubber, it is essentially the most important substance involved in the vulcanization reaction, along with accelerators and zinc white. However, the sulfur remains as a coarse particle,
If they are present in the rubber to be vulcanized, during vulcanization, the areas where coarse particles are present will locally become overvulcanized, and after vulcanization, post-recursion will proceed in these areas, resulting in aging of the rubber product5. It gets faster. Therefore, it is desirable that the sulfur be as fine a particle as possible, and currently, sulfur in the form of a fine powder of 200 to 300 mesh or more is normally used for dry rubber. Today, the most common method for producing powdered sulfur industrially is to grind bulk sulfur into powder using a crusher, and then classify the powder to collect a portion of a certain particle size.
特殊な方法としては、液状イオウを加圧して、ノズルか
ら押し出して霧状とし、これを冷却した広い室内にて急
冷する方法がある。これらの15方法においては、いず
れも粉塵爆発の危険があるので、前者においては、室は
チッ素あるいは炭酸ガスなどの不活性ガスを循環する必
要があるばかりでなく、微粉末を取扱うために粉塵公害
を起すおそれがあるため、特別の配慮をしなければなら
20ない。本発明は、これらのゴム用イオウ製造上の欠
点を除くと同時に、ゴム加工技術上待望されていた分散
性のすぐれたイオウを提供することを目的とするもので
ある。A special method is to pressurize liquid sulfur, force it out of a nozzle to form a mist, and rapidly cool it in a large, cooled room. In these 15 methods, there is a risk of dust explosion, so in the former case, not only is it necessary to circulate an inert gas such as nitrogen or carbon dioxide in the chamber, but also a dust explosion is required in order to handle fine powder. Because of the risk of causing pollution, special consideration must be taken. The object of the present invention is to eliminate these drawbacks in the production of sulfur for rubber, and at the same time provide sulfur with excellent dispersibility, which has been long-awaited in terms of rubber processing technology.
25この目的を達成するために鋭意研究の結果、イオウ
とワックスとをイオウの融点以上に加熱熔融し、かきま
ぜて均一となしつつ、冷却成型する成型イオウの製造方
法を見い出し、本発明を完成した。25 In order to achieve this objective, as a result of intensive research, we discovered a method for producing molded sulfur by heating and melting sulfur and wax above the melting point of sulfur, stirring them to make them homogeneous, and then cooling and molding them, thus completing the present invention. .
30本発明者らは、これとは別に、常温で固体のワック
スとこれより高い融点を有する粉状ゴム配合剤とを、該
ワックスの融点以上に加熱し、かきまぜて均一となしつ
つ冷却成型する成型ゴム配合剤の製造方法を見い出し、
先に特許出願した(公開35特許公報昭52−2259
3号)が、本発明は、粉状イオウではなく塊状イオウに
上記ワックスを添加し、イオウの融点以上に加熱し、同
様に処理することにより、粉砕工程が不要でしかも分散
性にすぐれたゴム用イオウを製造する方法を提供するも
のである。30 Separately, the present inventors heated a wax that is solid at room temperature and a powdered rubber compounding agent having a higher melting point above the melting point of the wax, stirred it to make it uniform, and then cooled and molded it. Discovered a method for manufacturing molded rubber compounds,
I filed a patent application first (Publication 35 Patent Publication 1982-2259)
No. 3), but in the present invention, the above-mentioned wax is added to bulk sulfur instead of powdered sulfur, heated above the melting point of sulfur, and treated in the same manner, thereby creating a rubber that does not require a pulverization step and has excellent dispersibility. The present invention provides a method for producing sulfur for industrial use.
この際、塊状イオウを加熱し融解さす必要から、塊状イ
オウに代えてはじめから液状イオウを用いてもよいこと
は勿論である。この方法によれば、製造中またはゴム工
場において使用中に、粉塵公害ないしは粉塵爆発を起す
おそれがなく、不活性ガスなどの副資材を使用せずに、
しかも従来の粉末イオウより分散性がすぐれ、取扱いや
すく流動性のよい(フリーフローインク)イオウを経済
的に製造することが可能である。本発明において使用す
る原料イオウは、蒸留イオウまたは石油化学によつて回
収されたイオウなどで、純度が従来用いられていたイオ
ウ程度のものなら、いずれも使用することができる。本
発明において、イオウに添加するワツクスとしては石油
から分離精製されるパラフインワツクス、マイクロクリ
スタリンワツクス、または一般の値物ロウ、動物ロウ、
鉱物ロウのほか、場合によつては合成ワツクスなどで加
硫反応ないしは加硫ゴムに対して悪影響をおよぼさない
ものなら何でも使用できるが、このうちマイクロクリス
タリンワツクスを使用する際、特に好ましい結果が得ら
れる。At this time, since it is necessary to heat and melt the bulk sulfur, it is of course possible to use liquid sulfur instead of the bulk sulfur. According to this method, there is no risk of causing dust pollution or dust explosion during manufacturing or use in a rubber factory, and there is no need to use auxiliary materials such as inert gas.
Furthermore, it is possible to economically produce sulfur that has better dispersibility than conventional powdered sulfur, is easy to handle, and has good fluidity (free-flow ink). The raw material sulfur used in the present invention may be distilled sulfur or sulfur recovered by petrochemistry, and any purity can be used as long as it has a purity comparable to conventionally used sulfur. In the present invention, the wax added to sulfur includes paraffin wax separated and refined from petroleum, microcrystalline wax, general valuable wax, animal wax,
In addition to mineral waxes, in some cases, synthetic waxes can be used, as long as they do not have an adverse effect on the vulcanization reaction or vulcanized rubber, but microcrystalline waxes are particularly preferred. Get results.
イオウに対するワツクスの使用割合は、重量比として通
常5%以下、最適には0.1〜3%の割合で添加する際
、ゴム用イオウとして好ましい製品が得られる。本発明
を実施するにあたり、粒状に成型するためには、たとえ
ば、液状イオウにワツクスを加え、かきまぜ両者が均一
に分散した状態を保ちながら半熔融状態になるまで冷却
したのち、押出し造粒する。When adding wax to sulfur in a weight ratio of usually 5% or less, most preferably 0.1 to 3%, a product preferable as sulfur for rubber can be obtained. In carrying out the present invention, in order to mold into granules, for example, wax is added to liquid sulfur, stirred and cooled to a semi-molten state while maintaining a uniformly dispersed state, and then extruded and granulated.
本発明の特徴は、ゴム用イオウを製造する際の多くの問
題点を解決したことにある。A feature of the present invention is that it solves many problems in producing sulfur for rubber.
すなわち、従来は微粉末にするために粉砕工程が必要で
あつたが、本発明においては、このような粉砕工程が全
くないので、粉塵公害を起す心配がなく衛生的であり、
またイオウの粉砕においては、粉砕機の過熱などにより
粉塵爆発を起す危険があるので、粉砕機を冷却したりあ
るいは不活性ガスを使用するが、本発明においては、か
かる配慮をすることも不要であり、火災爆発のおそれが
全くない。しかも、本発明は容易に連続的に実施するこ
とができる。すなわち、定量ポンプから一定時間に一定
量流れてくる流状イオウとワツクスとを混合機にて混和
しながら、半熔融状態になるまで冷却し、造粒機に供給
して成型し冷却することによつて、連続的に一定品質の
成型イオウを製造することができる。さらに、このよう
な連続的製造方法においては、液状イオウから30分以
内に成型イオウが得られるので、工賃も光熱費も通常の
ゴム用イオウ製造時の数分の一ですむので、経済的にも
有利である。また、本発明を実施するに必要な機械装置
は従来の粉末イオウの製造装置に比べはるかに小型であ
るため、所要面積の点からも有利である。さらに、ゴム
製品の製造工程においても、従来の粉末イオウを使用す
る場合は、粉塵公害が起きやすく、かつ、ホツパ一およ
び容器に付着するため、配合操作がやつかいであるばか
りでなく、秤量の誤差も生じやすいが、本発明に係るイ
オウはフリーフローインクの形状であるので、このよう
な欠点は全くみられない。That is, in the past, a pulverization process was required to make it into a fine powder, but in the present invention, such a pulverization process is not required at all, so there is no fear of causing dust pollution, and it is hygienic.
In addition, when pulverizing sulfur, there is a risk of a dust explosion due to overheating of the pulverizer, so the pulverizer is cooled or an inert gas is used, but in the present invention, such considerations are unnecessary. Yes, there is no risk of fire or explosion. Moreover, the present invention can be easily implemented continuously. In other words, the liquid sulfur and wax that flow in a certain amount at a certain time from a metering pump are mixed in a mixer and cooled until it becomes a semi-molten state, and then fed to a granulator to be molded and cooled. Therefore, molded sulfur of constant quality can be produced continuously. Furthermore, in this continuous production method, molded sulfur can be obtained from liquid sulfur within 30 minutes, so the labor and utility costs are a fraction of that of normal rubber sulfur production, making it economically viable. is also advantageous. Additionally, the mechanical equipment required to carry out the present invention is much smaller than conventional powdered sulfur manufacturing equipment, which is advantageous in terms of the area required. Furthermore, when conventional powdered sulfur is used in the manufacturing process of rubber products, it is easy to cause dust pollution and adheres to the hopper and container, making the blending operation difficult and weighing difficult. Although errors are likely to occur, since the sulfur according to the present invention is in the form of free-flowing ink, such defects are not observed at all.
その上、本発明により製造されたイオウは単なるイオウ
に比べ低温で融け始め、融点巾が広いので、普通の粉末
イオウより低温で短時間にゴムに分散するため、分散不
良を起す心配がなく使用することができ、ゴム用イオウ
として最適なものである。以上述べたように、本発明は
、液状イオウに加硫反応ないしは加硫ゴムの性質に悪影
響をおよぼさないワツクスを添加することによつて、粉
末化しなくとも均一にゴムに分散し、しかも取扱いやす
い形状のゴム用イオウを安全かつ衛生的に、また経済的
に製造せんとする新規なゴム用イオウの製造せんとする
新規なゴム用イオウの製造方法である。Furthermore, the sulfur produced by the present invention begins to melt at a lower temperature than simple sulfur and has a wider melting point range, so it can be dispersed into rubber at a lower temperature and in a shorter time than ordinary powdered sulfur, so it can be used without worrying about poor dispersion. It is the most suitable sulfur for rubber. As described above, the present invention enables liquid sulfur to be uniformly dispersed in rubber without being powdered by adding wax that does not adversely affect the vulcanization reaction or the properties of vulcanized rubber. This is a novel method for producing sulfur for rubber, which aims to produce sulfur for rubber in a form that is easy to handle safely, hygienically, and economically.
次に実施例を挙げて、本発明を具体的に説明する。Next, the present invention will be specifically explained with reference to Examples.
実施例 1
あらかじめ約120℃に加熱された液状イオウ5009
に かきまぜながらマイクロクリスタリンワツクス(融
点55℃)15f!を加え、混合熔融して両者が均一と
なるように攪拌しながら、半熔融状態になるまで冷却し
、押出式造粒機で造粒すると、89℃で融け始めるペレ
ツト状イオウ5079を得た。Example 1 Liquid sulfur 5009 preheated to about 120°C
Microcrystalline wax (melting point 55℃) 15f while stirring! was added, mixed and melted, and while stirring so that both were homogeneous, was cooled to a semi-molten state and granulated using an extrusion type granulator to obtain pellet-like sulfur 5079 that began to melt at 89°C.
実施例 2
固形イオウ5009とマイクロクリスタリンワツクス5
9を、約120℃に加熱し混合熔融し、両者が均一にな
るようにかきまぜ、攪拌をつづけながら半熔融状態にな
るまで冷却し、押出し造粒すると、109℃でとけ始め
るペレツト状のイオウ4909を得た。Example 2 Solid sulfur 5009 and microcrystalline wax 5
9 are mixed and melted by heating to about 120°C, stirred so that both are uniform, cooled to a semi-molten state while continuing to stir, and extruded and granulated to form pellet-shaped sulfur 4909 that starts to melt at 109°C. I got it.
実施例 3
液状イオウを1.0kg/Hr,マイクロクリスタリン
ワツクスを0.5kg/Hrの割合で、約120℃に加
熱された連続混合機(ニーダ一)に連続的に供給し、混
合熔融して均一になるまでかきまぜ、次いで、冷却され
た連続混合機に導入して半熔融状態で押出し造粒する。Example 3 Liquid sulfur was continuously supplied at a rate of 1.0 kg/Hr and microcrystalline wax at a rate of 0.5 kg/Hr to a continuous mixer (kneader 1) heated to about 120°C, and mixed and melted. The mixture is stirred until homogeneous, then introduced into a cooled continuous mixer, and extruded and granulated in a semi-molten state.
流動冷却して連続的に、74℃で融け始めるペレツト状
イオウを得た。実施例1〜3で合成したワツクスで成型
したイオウの分散性を試験するため未加硫の天然ゴム1
00g中にロール中で59のイオウを5分で混合し、1
回薄通しののちゴム中の分散不良粒子数を肉眼で判定し
た。結果を以下に示す。Continuous fluidized cooling yielded sulfur pellets that began to melt at 74°C. Unvulcanized natural rubber 1 was molded with the wax synthesized in Examples 1 to 3 to test the dispersibility of sulfur.
00g of sulfur was mixed in a roll for 5 minutes, and 1
After passing through the rubber several times, the number of poorly dispersed particles in the rubber was determined visually. The results are shown below.
以上により本発明は成型品であるにもかかわらず粉末イ
オウと同等の分散性の良好な成型イオウの製造であるこ
とが判明した。From the above, it has been found that the present invention can produce molded sulfur having good dispersibility equivalent to that of powdered sulfur even though it is a molded product.
Claims (1)
上に加熱し、かきまぜて均一となしつつ、冷却成型する
ことを特徴とする成型イオウの製造方法。1. A method for producing molded sulfur, which comprises heating sulfur and wax, which is solid at room temperature, above the melting point of sulfur, stirring the mixture to make it uniform, and then cooling and molding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8059075A JPS5914401B2 (en) | 1975-06-30 | 1975-06-30 | Method for manufacturing molded sulfur |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8059075A JPS5914401B2 (en) | 1975-06-30 | 1975-06-30 | Method for manufacturing molded sulfur |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS524495A JPS524495A (en) | 1977-01-13 |
| JPS5914401B2 true JPS5914401B2 (en) | 1984-04-04 |
Family
ID=13722544
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8059075A Expired JPS5914401B2 (en) | 1975-06-30 | 1975-06-30 | Method for manufacturing molded sulfur |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5914401B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090242165A1 (en) | 2008-03-25 | 2009-10-01 | Beitelman Leonid S | Modulated electromagnetic stirring of metals at advanced stage of solidification |
| JP2017014334A (en) * | 2015-06-29 | 2017-01-19 | 住友ゴム工業株式会社 | Manufacturing method of rubber composition |
-
1975
- 1975-06-30 JP JP8059075A patent/JPS5914401B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS524495A (en) | 1977-01-13 |
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