JPS5914402B2 - Method for producing granular sulfur - Google Patents
Method for producing granular sulfurInfo
- Publication number
- JPS5914402B2 JPS5914402B2 JP9878375A JP9878375A JPS5914402B2 JP S5914402 B2 JPS5914402 B2 JP S5914402B2 JP 9878375 A JP9878375 A JP 9878375A JP 9878375 A JP9878375 A JP 9878375A JP S5914402 B2 JPS5914402 B2 JP S5914402B2
- Authority
- JP
- Japan
- Prior art keywords
- sulfur
- rubber
- disulfide
- present
- molten state
- 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 55
- 229910052717 sulfur Inorganic materials 0.000 title claims description 54
- 239000011593 sulfur Substances 0.000 title claims description 54
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 238000002844 melting Methods 0.000 claims description 5
- 230000008018 melting Effects 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- AFZSMODLJJCVPP-UHFFFAOYSA-N dibenzothiazol-2-yl disulfide Chemical compound C1=CC=C2SC(SSC=3SC4=CC=CC=C4N=3)=NC2=C1 AFZSMODLJJCVPP-UHFFFAOYSA-N 0.000 claims description 2
- 229920001971 elastomer Polymers 0.000 description 12
- 239000005060 rubber Substances 0.000 description 12
- BWGNESOTFCXPMA-UHFFFAOYSA-N Dihydrogen disulfide Chemical compound SS BWGNESOTFCXPMA-UHFFFAOYSA-N 0.000 description 11
- 238000000034 method Methods 0.000 description 8
- 239000000428 dust Substances 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 230000005496 eutectics Effects 0.000 description 4
- 238000005469 granulation Methods 0.000 description 4
- 230000003179 granulation Effects 0.000 description 4
- 229920001021 polysulfide Polymers 0.000 description 4
- 239000005077 polysulfide Substances 0.000 description 4
- 150000008117 polysulfides Polymers 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 238000004073 vulcanization Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000002156 mixing 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
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920003052 natural elastomer Polymers 0.000 description 2
- 229920001194 natural rubber Polymers 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000010058 rubber compounding Methods 0.000 description 2
- -1 that is Polymers 0.000 description 2
- VZSRBBMJRBPUNF-UHFFFAOYSA-N 2-(2,3-dihydro-1H-inden-2-ylamino)-N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]pyrimidine-5-carboxamide Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)C(=O)NCCC(N1CC2=C(CC1)NN=N2)=O VZSRBBMJRBPUNF-UHFFFAOYSA-N 0.000 description 1
- 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
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 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
- 238000007796 conventional method Methods 0.000 description 1
- 229920003244 diene elastomer Polymers 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229920003049 isoprene rubber Polymers 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 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
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000012260 resinous material Substances 0.000 description 1
- 238000010057 rubber processing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 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
- 235000014692 zinc oxide Nutrition 0.000 description 1
- 239000011787 zinc oxide Substances 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のすぐれた成
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.
より詳しくはイオウとイオウ量の0.1〜5重量パーセ
ントのジベンゾチアジルジスルフイドを、イオウの融点
以上に加熱溶融し均一となしたるのち、半溶融状態にな
るまで冷却し押出し造粒することを特徴とする粒状イオ
ウの製造方法に係るものである。イオウはゴム配合剤と
して、ジエンゴム、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
ゴム製品の加硫において、促進剤および亜鉛華と共に、
5 本質的に加硫反応に関与する最も大切な物質である
。More specifically, sulfur and dibenzothiazyl disulfide in an amount of 0.1 to 5% by weight of sulfur are melted by heating to a temperature above the melting point of sulfur to make it homogeneous, and then cooled to a semi-molten state and extruded into granules. The present invention relates to a method for producing granular sulfur characterized by: Sulfur is used as a rubber compounding agent, together with accelerators and zinc white, in the vulcanization of diene rubber, that is, natural rubber or synthetic rubber products such as styrene-butadiene rubber, acrylonitrile-butadiene rubber, isoprene rubber, butadiene rubber, and butyl rubber.
5 Essentially the most important substance involved in the vulcanization reaction.
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、0はこの部分の後加
硫が進行して、ゴム製品の老化が早くなる。However, if sulfur is present in the rubber to be vulcanized as coarse particles, the area where the coarse particles are present will locally become overvulcanized during vulcanization, and after vulcanization, 0 will be post-vulcanized in this area. This progresses, causing the rubber products to age faster.
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。15今日、粉末イオウを工業的に製造する最も
普通の方法は、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。Therefore, it is desirable that sulfur be as fine a particle as possible, and currently, sulfur for dry rubber is
A fine powder of 200 to 300 mesh or more is used. 15 Today, the most common method for producing powdered sulfur industrially is to grind bulk sulfur into powder using a grinder.
This is a method of classifying this and collecting parts of a certain particle size.
特殊な方法としては、液状となし、これを冷却した広い
室内にて急冷する方法がある。これク0 らの方法にお
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、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ので、特別の配慮をしなけ
ればなら25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ともに、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 make it into a liquid and rapidly cool it in a large, cooled room. In both of these 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, but also the chamber is used to handle fine powder. To,
Since there is a risk of causing dust 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 to provide sulfur with excellent dispersibility, which has been long-awaited in terms of rubber processing technology.
30この目的を達成するために、本発明者らは先に、イ
オウとワックスとをイオウの融点以上に加熱溶融し、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
造方法を発明したが、さらに研究を重ねた結果、イオウ
を少量のジベンゾチアジル35 ジスルフィドと共に混
合溶融したのち、半溶融状態で押出し造粒することによ
り、ゴムヘの練り込みが容易で、しかも分散性のすぐれ
た成型イオウ=−が得られることを見い出し、本発明を
完成した。30 In order to achieve this objective, the present inventors previously invented a method for producing molded sulfur in which sulfur and wax are melted by heating to a temperature above the melting point of sulfur, stirred to make it uniform, and then cooled and molded. As a result of further research, it was found that by mixing and melting sulfur with a small amount of dibenzothiazyl 35 disulfide, and then extruding and granulating it in a semi-molten state, molded sulfur that can be easily kneaded into rubber and has excellent dispersibility was created. It was discovered that =- could be obtained, and the present invention was completed.
従来、イオウとジベンゾチアシルジスルフィドとを共融
反応させ、分子化合物を形成させた例として、日本ゴム
協会誌25巻138頁があり、さらに、得られた樹脂状
共融物をそのままゴムに配合し、加硫剤として試験し(
同164頁)、またゴムに対する可塑化作用について報
告(同166頁)したものがある。しかしながら、この
例においては、ジベンゾチアシルジスルフィドの添加量
が多いため、イオウとの共融により得られるものは、樹
脂状物質であり、本発明のように造粒成型することは不
可能である。本発明は、これらの公知の文献とは異なり
、イオウに対し0.1〜5.0重量パーセントの少量の
ジベンゾチアシルジスルフィドを添加して混合溶融した
ものについては、半溶融状態において、押出し造粒が可
能であることの知見に基づいてなされたものである。Conventionally, there is an example of eutectic reaction of sulfur and dibenzothiacyl disulfide to form a molecular compound, as described in the Journal of the Japan Rubber Association, Vol. 25, p. 138, and furthermore, the resulting resinous eutectic product is blended into rubber as it is. and tested as a vulcanizing agent (
There is also a report on the plasticizing effect on rubber (p. 166). However, in this example, since the amount of dibenzothiacyl disulfide added is large, what is obtained by eutectic synthesis with sulfur is a resinous material, and it is impossible to granulate it as in the present invention. . The present invention differs from these known documents in that a small amount of dibenzothiacyl disulfide is added to sulfur in an amount of 0.1 to 5.0% by weight and then mixed and melted. This was done based on the knowledge that grains are possible.
このことは、イオウに対するジベンゾチアシルジスルフ
ィドの添加量が多いときは、両者を加熱溶融する際、イ
オウのほとんどすべてが、ジベンゾチアシルジスルフィ
ドと反応して、種々の多硫化物を形成し、樹脂状物質が
得られるのに対し、添加量が少い場合においては、イオ
ウの一部がジベンゾチアシルジスルフィドと反応し多硫
化物を形成し、次いで、この多硫化物とイオウとが共融
物を形成するものと考えられる。This means that when the amount of dibenzothiacyl disulfide added to sulfur is large, when both are heated and melted, almost all of the sulfur reacts with dibenzothiacyl disulfide to form various polysulfides, resulting in resin However, when the amount added is small, part of the sulfur reacts with dibenzothiacyl disulfide to form a polysulfide, and then this polysulfide and sulfur form a eutectic product. It is thought to form a
さらに、造粒に際しては、ここに生じた多硫化物があた
かも結合剤の如く有効に作用するものと推察される。し
かも、驚くべきことには、このようにして得られた成型
イオウは、従来使用されている微粉末イオウに比べ、ゴ
ムに配合した際、同等もしくはそれ以上の分散性を有し
ていることが判明した。さらに、本発明の特徴とすると
ころは、従来の粉末イオウ製造時に必須工程であつた粉
砕工程が全く不用であるため、粉塵爆発を起す危険がな
く、また、粉塵公害を起す心配もなく衛生的にゴム用イ
オウを製造することができる。その上、本発明により得
られた成型イオウは、ゴム製品の製造工程において使用
する際にも多くの長所を有する。Furthermore, during granulation, it is presumed that the polysulfide produced here acts effectively as if it were a binder. Moreover, surprisingly, the molded sulfur obtained in this way has the same or better dispersibility when blended into rubber than the conventionally used fine powder sulfur. found. Furthermore, the present invention is characterized by completely eliminating the need for a crushing process, which was an essential process in the production of powdered sulfur in the past, so there is no risk of dust explosion, and there is no risk of dust pollution, making it a hygienic process. can produce sulfur for rubber. Moreover, the molded sulfur obtained according to the invention has many advantages when used in the manufacturing process of rubber products.
すなわち、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
ために、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。本発明において使用される原料イオウは、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、純度が従来ゴム用として使用されていた程度のもの
なら、いずれも使用することができ、固形イオウのほか
製造時に加熱溶解さす必要から、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。In other words, when using conventional powdered sulfur, it is easy to cause dust pollution, and because it adheres to the hopper and container, not only is the mixing operation difficult, but it also tends to cause errors in weighing. Since the sulfur according to the invention is in the form of a free-flowing ink, no such drawbacks are observed. The raw material sulfur used in the present invention may be distilled sulfur or sulfur recovered through petrochemistry, as long as its purity is at the level conventionally used for rubber. In addition, it is of course possible to use liquid sulfur from the beginning since it is necessary to heat and melt it during production.
本発明を有利に実施するには、イオウに対し、0.1〜
5.0重量パーセントの有機ジスルフイド化合物を添加
し、120〜140℃に加熱し、30分〜1時間かきま
ぜながら混合溶融し、均一となしたるのち、半溶融状態
になるまで冷却し、押出式造粒機を用い、常法により押
出し造粒する。To carry out the invention advantageously, the sulfur
Add 5.0% by weight of an organic disulfide compound, heat to 120 to 140°C, mix and melt while stirring for 30 minutes to 1 hour, make it homogeneous, cool to a semi-molten state, and extrude. Extrusion and granulation are carried out using a granulator using a conventional method.
次に実施例を挙げて、本発記を説明する。実施例 1
固形イオウ1kgをステンレス製混合器(ニーダ一)に
入れ、120〜125℃に加熱し融解させ、かきまぜな
がらジベンゾチアシルジスルフィド309を加え、同温
度で30分間混合溶融したのち、95〜100℃に冷却
し、半溶融体態において押出式造粒機により造粒し、流
動冷却すると、とけ始めが95℃の粒状イオウ1010
9が得られた。Next, the present statement will be explained by giving examples. Example 1 1 kg of solid sulfur was placed in a stainless steel mixer (kneader 1), heated to 120-125°C to melt it, added dibenzothiacyl disulfide 309 while stirring, mixed and melted at the same temperature for 30 minutes, and then heated to 120-125°C. When cooled to 100°C, granulated in a semi-molten state using an extrusion type granulator, and cooled with fluidization, granular sulfur 1010 melts at 95°C.
9 was obtained.
実施例 2
あらかじめ約130℃に加熱された液状イオウ100g
に、かきまぜながらベンゾチアシルジスルフィド109
を加え、同温度で30分間加熱溶融すると両者は均一な
液層を形成する。Example 2 100g of liquid sulfur preheated to about 130°C
Add benzothiacil disulfide 109 while stirring.
When added and melted by heating at the same temperature for 30 minutes, both forms a uniform liquid layer.
次いで、これを液状イオウ900f1に加え、さらに3
0分間かきまぜながら混合溶融したのち、半溶融状態に
なるまで放冷し、押出式造粒機により造粒し、流動冷却
すると、とけ始めが99℃の粒状イオウ9909が得ら
れた。比較例 1
シベンゾチアジルジスルフイドを0.8gに変えた他は
、実施例1に準じて行なつた。Next, add this to 900f1 of liquid sulfur, and add 3
After mixing and melting with stirring for 0 minutes, the mixture was allowed to cool to a semi-molten state, granulated using an extrusion type granulator, and fluidized and cooled to obtain granular sulfur 9909 that melted at 99°C. Comparative Example 1 The procedure of Example 1 was followed except that cybenzothiazyl disulfide was changed to 0.8 g.
半溶融状態で押出造粒を行なつたが、イオウはフレ.−
ク状となつた。比較例 2
ジベンゾチアシルジスルフィドを90gに変えた他は実
施例1に準じて行なつた。Extrusion granulation was performed in a semi-molten state, but the sulfur was flabby. −
It turned into a square shape. Comparative Example 2 The procedure of Example 1 was followed except that the amount of dibenzothiacyl disulfide was changed to 90 g.
半溶融状態で押出造粒を行なつたが粒状化せず、イオウ
は溶融状態のまま塊状化した。実施例.比較例
イオウの分散性を試験するため、天然ゴム1009中に
ロール中で51のイオウを5分で混合し、1回薄通しの
のち肉眼で判定した。Although extrusion granulation was carried out in a semi-molten state, the sulfur did not become granulated, and the sulfur remained in a molten state and became agglomerated. Example. Comparative Example To test the dispersibility of sulfur, sulfur 51 was mixed into natural rubber 1009 in a roll for 5 minutes, passed through once, and then judged visually.
その結果を以下に記す。以上により本発明は分散性の良
好な成型イオウの製造方法であり、本願特許請求の範囲
内の添加量によつてのみ粒状品であるにも係わらず粉末
イオウと同等な文散性の良好なイオウが得られることが
判明した。The results are described below. As described above, the present invention is a method for producing molded sulfur with good dispersibility, and even though it is a granular product, it can be produced with good dispersibility equivalent to that of powdered sulfur by adding the amount within the scope of the claims of the present patent. It turns out that sulfur can be obtained.
Claims (1)
ベンゾチアジルジスルフイドをイオウの融点以上に加熱
溶融し均一となしたるのち、半溶融状態になるまで冷却
し押出し造粒することを特徴とする粒状イオウの製造方
法。1 Sulfur and dibenzothiazyl disulfide in an amount of 0.1 to 5% by weight based on the sulfur content are melted by heating to a temperature above the melting point of sulfur to make it homogeneous, and then cooled to a semi-molten state and extruded and granulated. Characteristic method for producing granular sulfur.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9878375A JPS5914402B2 (en) | 1975-08-14 | 1975-08-14 | Method for producing granular sulfur |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9878375A JPS5914402B2 (en) | 1975-08-14 | 1975-08-14 | Method for producing granular sulfur |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5222593A JPS5222593A (en) | 1977-02-19 |
| JPS5914402B2 true JPS5914402B2 (en) | 1984-04-04 |
Family
ID=14228954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9878375A Expired JPS5914402B2 (en) | 1975-08-14 | 1975-08-14 | Method for producing granular sulfur |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5914402B2 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6113801A (en) * | 1984-06-29 | 1986-01-22 | Fujitsu Ltd | Transmission and reception branching filter |
| JPS6115401A (en) * | 1984-06-30 | 1986-01-23 | Murata Mfg Co Ltd | Distributed constant type filter |
| JPS6152003A (en) * | 1984-08-21 | 1986-03-14 | Murata Mfg Co Ltd | Dielectric filter |
| JPS6197205U (en) * | 1984-12-03 | 1986-06-21 | ||
| JPS62235801A (en) * | 1986-04-05 | 1987-10-16 | Fuji Elelctrochem Co Ltd | Incorporated type dielectric multicoupler |
| JPS6354802A (en) * | 1986-08-25 | 1988-03-09 | Oki Electric Ind Co Ltd | Dielectric filter |
| JPS6340009U (en) * | 1986-09-02 | 1988-03-15 | ||
| JPH05183308A (en) * | 1991-12-27 | 1993-07-23 | Uniden Corp | Dielectric filter |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5833500A (en) * | 1995-03-30 | 1998-11-10 | Yazaki Corporation | Terminal fixture and a method of manufacturing the same |
| JP3115805B2 (en) * | 1995-09-14 | 2000-12-11 | 矢崎総業株式会社 | Terminal fittings and method of manufacturing terminal fittings |
-
1975
- 1975-08-14 JP JP9878375A patent/JPS5914402B2/en not_active Expired
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6113801A (en) * | 1984-06-29 | 1986-01-22 | Fujitsu Ltd | Transmission and reception branching filter |
| JPS6115401A (en) * | 1984-06-30 | 1986-01-23 | Murata Mfg Co Ltd | Distributed constant type filter |
| JPS6152003A (en) * | 1984-08-21 | 1986-03-14 | Murata Mfg Co Ltd | Dielectric filter |
| JPS6197205U (en) * | 1984-12-03 | 1986-06-21 | ||
| JPS62235801A (en) * | 1986-04-05 | 1987-10-16 | Fuji Elelctrochem Co Ltd | Incorporated type dielectric multicoupler |
| JPS6354802A (en) * | 1986-08-25 | 1988-03-09 | Oki Electric Ind Co Ltd | Dielectric filter |
| JPS6340009U (en) * | 1986-09-02 | 1988-03-15 | ||
| JPH05183308A (en) * | 1991-12-27 | 1993-07-23 | Uniden Corp | Dielectric filter |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5222593A (en) | 1977-02-19 |
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