JPS5912712B2 - Remeltable asphalt powder and its manufacturing method - Google Patents
Remeltable asphalt powder and its manufacturing methodInfo
- Publication number
- JPS5912712B2 JPS5912712B2 JP453580A JP453580A JPS5912712B2 JP S5912712 B2 JPS5912712 B2 JP S5912712B2 JP 453580 A JP453580 A JP 453580A JP 453580 A JP453580 A JP 453580A JP S5912712 B2 JPS5912712 B2 JP S5912712B2
- Authority
- JP
- Japan
- Prior art keywords
- asphalt
- powder
- remeltable
- materials
- various
- 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
- 239000010426 asphalt Substances 0.000 title claims description 50
- 239000000843 powder Substances 0.000 title claims description 34
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000000203 mixture Substances 0.000 claims description 20
- 239000003054 catalyst Substances 0.000 claims description 7
- 238000000227 grinding Methods 0.000 claims description 7
- 229920005672 polyolefin resin Polymers 0.000 claims description 7
- 238000010298 pulverizing process Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims 1
- 239000000463 material Substances 0.000 description 23
- 238000013329 compounding Methods 0.000 description 16
- 230000003647 oxidation Effects 0.000 description 13
- 238000007254 oxidation reaction Methods 0.000 description 13
- 239000003795 chemical substances by application Substances 0.000 description 11
- -1 compound compound Chemical class 0.000 description 7
- 229920005989 resin Polymers 0.000 description 7
- 239000011347 resin Substances 0.000 description 7
- 238000002156 mixing Methods 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910001882 dioxygen Inorganic materials 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 239000003973 paint Substances 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 230000035945 sensitivity Effects 0.000 description 3
- 238000004078 waterproofing Methods 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000012772 electrical insulation material Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229910052751 metal Chemical class 0.000 description 2
- 239000002184 metal Chemical class 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 150000004706 metal oxides Chemical class 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000012744 reinforcing agent Substances 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000005995 Aluminium silicate Substances 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000012615 aggregate Substances 0.000 description 1
- 235000012211 aluminium silicate Nutrition 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000006356 dehydrogenation reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical class [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 235000012254 magnesium hydroxide Nutrition 0.000 description 1
- 238000010299 mechanically pulverizing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
- Working-Up Tar And Pitch (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】
本発明は再溶融性アスファルト粉末、その製法及びその
利用に関し、とくに、室温で流動性良好な乾燥粉末状態
を呈し且つ加熱により例えば約100℃以上の温度で再
溶融可能であつて、たとえば、燃料、燃料配合材料、各
種結合剤、結合剤配合材料、各種防水剤、防水剤配合材
料、各種舗装材料、舗装材配合材料、各種充填材、充填
材配合材料、各種補強剤、補強剤配合材料、各種ゴム類
配合材料、各種耐振材、耐振材配合材料、各種塗料、塗
料配合材料、電気絶縁材、電気絶縁材配合材料、その他
のアスファルト類の従来用途分野を包含して新しい用途
分野にわたる広汎な用途分野において、優れた有用性を
示し且つ取扱い、貯蔵、運搬などが著しく容易なユニー
クな特性を有するアスファルト粉末、その製法ならびに
利用に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a remeltable asphalt powder, a method for producing the same, and its use, and in particular, the present invention relates to a remeltable asphalt powder, a method for producing the same, and a use thereof, and in particular, a powder that exhibits a dry powder state with good fluidity at room temperature and can be remelted by heating at a temperature of about 100° C. or higher, for example. For example, fuel, fuel compounding materials, various binders, binder compounding materials, various waterproofing agents, waterproofing compounding materials, various paving materials, pavement compounding materials, various fillers, filler compounding materials, various reinforcements. This includes conventional application fields for asphalt, such as additives, reinforcing agent compound materials, various rubber compound materials, various vibration-resistant materials, vibration-proof compound compound materials, various paints, paint compound materials, electrical insulation materials, electrical insulation compound compound materials, and other asphalt materials. The present invention relates to an asphalt powder that has unique properties that make it extremely useful in a wide range of new and new fields of application, and that makes it extremely easy to handle, store, transport, etc., as well as its preparation and use.
更に詳しくは、本発明は強酸化処理アスファルト類とオ
レフィン系樹脂類とを含有する溶融混合物を粉末化して
なる再溶融性アスファルト粉末、5 その製法ならびに
利用に関する。More specifically, the present invention relates to a remeltable asphalt powder obtained by pulverizing a molten mixture containing strongly oxidized asphalts and olefin resins, 5, and its manufacturing method and utilization.
天然アスファルト、ストレートアスファルト、ブローン
アスフアルト、カットバックアスファルトなど各種アス
ファルト類が知られており、広い分野に利用されている
が、アスファルト類は高い10感温性と強い粘結性を本
来有する物質であるため、その再溶融性を実質的に失う
ことなしに、これを室温において自由流動性を示す乾燥
粉末とすることは至難であり、従来、その例を見ないの
が実情である。Various asphalts such as natural asphalt, straight asphalt, blown asphalt, and cutback asphalt are known and used in a wide range of fields, but asphalts are substances that inherently have high temperature sensitivity and strong caking properties. Therefore, it is extremely difficult to make it into a dry powder that exhibits free-flowing properties at room temperature without substantially losing its remeltability, and the reality is that there has been no example of this in the past.
15−般に、軟化点が低く粘結性を有する物質の機械的
粉末化処理に際しては、どのような手段を採用しても被
粉末化物質と破砕機構との間の摩擦発熱により、被粉末
化物質の軟化ないし溶融が回避できないため、所望の粉
末を得ることは実際上でク0 きないのが普通である。15-Generally, when mechanically pulverizing a substance with a low softening point and caking property, no matter what method is adopted, frictional heat generation between the material to be pulverized and the crushing mechanism causes the pulverization to occur. Since softening or melting of the compound cannot be avoided, it is usually practically impossible to obtain the desired powder.
このような物質の粉末化のために、たとえば凍結粉砕手
段が採用できるが、手段及び装置上の不利益に加えて、
得られた粉末化物は再び室温にもどると、元の粘結性状
態に復元するため再凝結ないし再粘結して塊状となり、
ク5 粉末化の目的を失うに至る。この現象は、たとえ
ば貯蔵中に加わる負荷重状態では一層甚だしくなる。例
えば、アスファルト類としては最も感温性の低い部類に
属するブローンアスフアルト(針入度3033−25℃
、100θ、5秒:軟化点105℃)の塊状固体試料を
固定・・ンマー式粉砕機を用いて粉末化処理することに
より、ブローンアスフアルト粉末を得ようとすると、粉
砕による発熱のため、一旦粉末化したブローンアスフア
ルトは互いに再35粘結凝集して再び塊状となり、粉末
化の目的を達することができない。For pulverization of such substances, for example, freeze-grinding means can be employed, but in addition to the disadvantages in terms of means and equipment,
When the obtained powdered product returns to room temperature, it re-condenses or re-agglomerates to restore its original cohesive state and becomes a lump.
H5: The purpose of powdering is lost. This phenomenon becomes even more severe under heavy loads, for example during storage. For example, blown asphalt, which has the lowest temperature sensitivity among asphalts (penetration: 3033-25℃)
, 100θ, 5 seconds: Softening point: 105°C) When attempting to obtain blown asphalt powder by pulverizing a lumpy solid sample with a fixed... The blown asphalt that has been pulverized will coagulate and coagulate with each other again and become lumpy, making it impossible to achieve the purpose of pulverization.
ブローンアスフアルトより感温性のより大きいストレー
トアスファルトではハη−この傾向は一層甚だしく、到
底、機械的粉末化を行うことはできない。In straight asphalt, which is more sensitive to temperature than blown asphalt, this tendency is even more severe, and mechanical pulverization cannot be performed at all.
一方、アスフアルト残渣を乾溜炭化した所謂1オイルコ
ークス1は室温で安定な粉末となるが、このものは、ア
スフアルトの成分組成が変化し、従つてその感温性を失
つていて、加熱再溶融物とすることはできない。On the other hand, so-called oil coke 1 produced by dry distillation carbonization of asphalt residue becomes a powder that is stable at room temperature, but this product has a change in the asphalt component composition, has therefore lost its temperature sensitivity, and cannot be heated and remelted. It cannot be made into a thing.
本発明者等は、上述のように、従米その再溶融性を実質
的に失うことなく、しかも室温において安定な粉末とす
ることが、実際上、できなかつたアスフアルト類の粉末
化物を提供すべく研究を行つてきた。As mentioned above, the present inventors aimed to provide a powdered product of asphalts that does not substantially lose its remeltability and that is practically impossible to form into a powder that is stable at room temperature. I've been doing research.
その結果、アスフアルト類を強酸化処理、好ましくは触
媒の存在下に空気酸化処理した強酸化処理アスフアルト
類に、オレフイン系樹脂を助剤として溶融条件下に配合
した溶融混合物は、室温で容易に粉末化することができ
て、安定な粉末を形成し、且つこの粉末は加熱により、
たとえば約100℃以上に加熱することにより容易に再
溶融することができ、前記したような広い利用分野にお
いて、取扱い、貯蔵、移送、作業性などの優れた粉末流
動性を示す再溶融性アスフアルト粉末としてユニークな
特性を有することを発見した。As a result, a molten mixture obtained by blending asphalt with strong oxidation treatment, preferably air oxidation treatment in the presence of a catalyst, with an olefinic resin as an auxiliary agent under melting conditions, can be easily powdered at room temperature. can be oxidized to form a stable powder, and this powder can be oxidized by heating.
For example, remeltable asphalt powder that can be easily remelted by heating to about 100°C or higher and exhibits excellent powder fluidity in handling, storage, transportation, workability, etc. in the wide range of applications mentioned above. discovered that it has unique properties.
従つて、本発明の目的は、室温で安定な粉末状態を保持
でき、加熱再溶融可能であつて、広い利用分野において
有用な再溶融性アスフアルト粉末を提供するにある。本
発明の他の目的は、このような再溶融性アスフアルト粉
末を工業的に有利且つ安価に提供できる製法を提供する
にある。Therefore, an object of the present invention is to provide a remeltable asphalt powder that can maintain a stable powder state at room temperature, can be remelted by heating, and is useful in a wide range of applications. Another object of the present invention is to provide a manufacturing method that is industrially advantageous and can provide such remeltable asphalt powder at low cost.
本発明の上記諸目的及び更に多くの他の目的ならびに利
点は、以下の記載から一層明らかとなるであろう。The above objects and many other objects and advantages of the present invention will become more apparent from the following description.
本発明の再溶融性アスフアルト粉末は、たとえば、アス
フアルト類を触媒の存在下に強酸化処理し、得られた強
酸化処理アスフアルト類とオレフイン系樹脂類を含有す
る溶融混合物を形成し、冷却したのち粉末化処理するこ
とにより製造することができる。The remeltable asphalt powder of the present invention can be obtained, for example, by subjecting asphalt to strong oxidation treatment in the presence of a catalyst, forming a molten mixture containing the obtained strongly oxidized asphalt and olefinic resin, and cooling the mixture. It can be manufactured by powdering.
上記強酸化処理は、たとえば金属酸化物や金属塩類の如
き酸化触媒の存在下に、原料アスフアルト類が液状なる
温度条件下で、原料アスフアルト類と分子状酸素たとえ
ば空気とを接触せしめることにより行うことができる。The above-mentioned strong oxidation treatment may be carried out by bringing the raw material asphalt into contact with molecular oxygen, such as air, in the presence of an oxidation catalyst such as a metal oxide or metal salt, and under temperature conditions such that the raw material asphalt is in a liquid state. I can do it.
分子状酸素もしくは分子状酸素含有ガスが利用でき、空
気、酸素、酸素と不活性ガス混合物などを例示すること
ができる。又、上記酸化触媒の例としては、CuO、A
t2O3,、P2O5、Atct3、FeCl3・6H
201At2(SO4)3などの如き金属酸化物もしく
は金属塩類を例示することができる。この酸化処理は、
形成される強酸化処理アスフアルト類の軟化点が約10
0℃以上に増大するまで行うのが好ましく、反応温度及
び時間は、この目安に従つて、適宜に選択実施すること
ができる。このような強酸化処理によつて、単なる空気
酸化では到達し難い充分な酸化処理が行われてアスフア
ルト類の脱水素重縮合反応が進行し且つ又複雑な三次元
的網状構造形成反応が生ずるものと推測される軟化点の
上昇が生ずる。Molecular oxygen or a molecular oxygen-containing gas can be used, and examples include air, oxygen, and a mixture of oxygen and an inert gas. Further, examples of the above-mentioned oxidation catalyst include CuO, A
t2O3,, P2O5, Atct3, FeCl3・6H
Examples include metal oxides or metal salts such as 201At2(SO4)3. This oxidation treatment
The softening point of the strongly oxidized asphalt that is formed is approximately 10
It is preferable to carry out the reaction until the temperature increases to 0° C. or higher, and the reaction temperature and time can be appropriately selected and carried out according to this guideline. Through such strong oxidation treatment, a sufficient oxidation treatment that is difficult to achieve with simple air oxidation is carried out, and the dehydrogenation polycondensation reaction of asphalts proceeds, and a complex three-dimensional network structure formation reaction occurs. This is thought to result in an increase in the softening point.
しかしながら、この状態では、なお不満足であつて、こ
のような強酸化処理アスフアルト類とオレフイン系樹脂
との溶融混合物とすることによつて、本発明のユニーク
な再溶融性アスフアルト粉末とすることができる。上述
のようにして得ることのできる強酸化処理アスフアルト
類とオレフイン系樹脂類との溶融混合物の形成は、両者
が溶融状態で、できるだけ均一に混合できる任意の手段
で行うことができる。However, this state is still unsatisfactory, and by forming a molten mixture of such strongly oxidized asphalt and olefin resin, the unique remeltable asphalt powder of the present invention can be obtained. . The molten mixture of strongly oxidized asphalt and olefinic resin that can be obtained as described above can be formed by any means that can mix them as uniformly as possible while they are in a molten state.
望むならば、上記酸化処理工程においてオレフイン系樹
脂類を配合し、酸化処理と溶融混合物の形成を同時的に
行うこともできる。形成された溶融混合物は放冷もしく
は積極的に冷却して適当な粉末化手段により破砕するこ
とにより所望の粒子サイズの粉末状製品とすることがで
き、更に、望むならば、篩分けすることができる。粉末
化処理手段は適宜に選択でき、工業的に有利には、機械
的粉砕手段ないし磨砕手段を採用することができる。粉
末粒子サイズは、所望により微粉状態から細粒、粗粒、
粒状などの状態にわたつて適宜に選択して粉末化するこ
とができる。更に、前述の酸化処理、溶融混合物形成処
理、該混合物形成後などの任意の工程で、乾燥助剤もし
くは最終用途における助燃、増量、充填、その他の配合
材料として役立つ有機もしくは無機質配合材料を加える
ことができる。このような配合材料の例としては、オガ
クズ類、モミガラ類、ワラ類、パルプ類、廃紙廃布パル
プ類、その他のセルロース系材料やコークス、石炭類な
どの如き可燃性材料、クレー、カオリン、ベントナイト
、シラス、火山灰、焼成ビル石、砂類、破砕石類その他
の粘土質乃至鉱物質充填材料などを例示することができ
る。この際、利用するオレフイン系樹脂類の例としては
、エチレン系重合体もしくは共重合体樹脂類、その他各
種α−オレフイン系重合体もしくは共重合体類、あるい
はこれらのブレンド物、更にはこれらと他樹脂との混合
物などを例示することができ、これらの中でもエチレン
系樹脂類の利用が好ましい。If desired, olefinic resins can be blended in the oxidation treatment step, and the oxidation treatment and formation of the molten mixture can be performed simultaneously. The formed molten mixture can be allowed to cool or actively cooled and crushed by suitable powdering means to give a powdered product of the desired particle size and, if desired, sieved. can. The powdering treatment means can be appropriately selected, and mechanical crushing means or grinding means can be employed if it is industrially advantageous. Powder particle size varies from fine powder to fine particles, coarse particles, and
It can be suitably selected from a range of granular and other forms and pulverized. Additionally, at any step such as the aforementioned oxidation treatment, molten mixture formation treatment, or after said mixture formation, organic or inorganic compounding materials may be added to serve as drying aids or combustion aids, bulking, filling, or other compounding materials in the end use. I can do it. Examples of such blended materials include sawdust, rice husk, straw, pulp, waste paper and cloth pulp, other cellulosic materials, coke, combustible materials such as coal, clay, kaolin, etc. Examples include bentonite, shirasu, volcanic ash, calcined building stone, sand, crushed stone, and other clay or mineral filling materials. In this case, examples of olefin resins to be used include ethylene polymers or copolymer resins, various other α-olefin polymers or copolymers, blends thereof, and others. Examples include mixtures with resins, and among these, it is preferable to use ethylene resins.
これらのオレフイン系樹脂類は粉末状態で利用してもよ
いし、或はこれら樹脂類の成形品スクラツプの如き廃棄
物の破細物も同様に利用でき、コストの面から有利であ
る。このようなオレフイン系樹脂類の配合量は適宜に選
択でき、たとえば、強酸化処理アスフアルト類100重
量部に対して約50重量部程度までの配合量を例示でき
、好ましくは約10〜約40重量部程度の配合量が採用
できる。上述のようにして得ることのできる本発明の再
溶融性アスフアルト粉末は、広い利用分野において、取
扱い性及び作業性の優れた粉末アスフアルトとして有利
に利用できる。These olefin resins may be used in powder form, or shredded waste products such as molded product scraps of these resins may be used as well, which is advantageous from a cost standpoint. The blending amount of such olefin resins can be selected as appropriate, and for example, the blending amount can be up to about 50 parts by weight, preferably about 10 to about 40 parts by weight, per 100 parts by weight of the strongly oxidized asphalt. A blending amount of approximately 1.5 parts can be adopted. The remeltable asphalt powder of the present invention, which can be obtained as described above, can be advantageously used as powdered asphalt with excellent handling and workability in a wide range of fields of application.
例えば、約0.1mf!Lもしくはそれ以下の微粉状態
に粉末化して、粉体燃焼炉燃料として利用したり、或は
又、重油などに混合してオイル・バーナー方式の噴射燃
焼炉燃料として利用したり、更に又、例えば、粗粒、粒
状、それらの集合物などの状態でそのまま燃料としたり
、或は前記例示の如き可燃性材料、各種助燃剤、カルシ
ウムやマグネシウムの水酸化物、酸化物などの如き硫黄
成分捕捉剤等の配合材料と混合しもしくは混合せずに、
任意の形状に加熱成形して固形燃料として利用すること
もできるし、練炭・豆炭類の配合燃料として利用するこ
ともできる。For example, about 0.1mf! It can be pulverized into a fine powder of L or less and used as a fuel for a powder combustion furnace, or it can be mixed with heavy oil etc. and used as a fuel for an oil burner type injection combustion furnace. , in the form of coarse particles, granules, or aggregates thereof, or as combustible materials such as those listed above, various combustion improvers, and sulfur component scavengers such as calcium and magnesium hydroxides and oxides. With or without mixing with other compounding materials,
It can be heat-molded into any shape and used as a solid fuel, or it can be used as a blended fuel for briquettes and charcoal charcoal.
更に又、木質チツプなどと混合したのち、所望の板状体
やプロツク状体などの形状に加熱加圧成形して耐水性ボ
ードやプロツク類として利用することができるし、或は
又、紙、布帛などの間に散布したのち熱カレンダーで加
熱圧着させて、従来の溶融アスフアルトコート法に比し
て簡易且つ迅速なアスファルトループインク加工に利用
することもできるし、又更に、道路舗装、防水壁工事な
どに際して、所望の骨材類と混合し、加熱転圧処理して
、従来の溶融もしくはカツトバツクアスフアルト法によ
る施工に比して、はるかに容易な施工手段及び優れた作
業性をもつて、舗装、防水加工などを行うのに利用する
こともできる。更に、各種の結合剤、その配合剤、各種
の充填剤、その配合剤、各種の補強剤、その配合剤、各
種ゴム類の配合剤、車輌類の耐振剤、その配合虱アスフ
アルト系塗料、その配合剤、電気絶縁材、その配合剤な
どとして、更に、廃棄物焼却炉用助燃剤、植物生育のた
めの土壌改良剤、湿地や軟弱地盤の土質改良剤、断熱剤
、それらの配合剤などとしても、優れた作業性及び取扱
い容易性をもつて利用できる。Furthermore, after mixing with wood chips etc., it can be molded under heat and pressure into the desired shape of a board or block to be used as a water-resistant board or block. Alternatively, it can be used as a water-resistant board or block. It can also be used for asphalt loop ink processing, which is simpler and faster than the conventional molten asphalt coating method, by spraying it between fabrics, etc. and then heating and pressing it with a thermal calendar.It can also be used for road paving, waterproof walls, etc. When carrying out construction work, it is mixed with the desired aggregates, heated and rolled, and has a much easier construction method and superior workability than the conventional melting or cutback asphalt methods. It can also be used for paving, waterproofing, etc. Furthermore, various binders, compounding agents thereof, various fillers, compounding agents thereof, various reinforcing agents, compounding agents thereof, compounding agents of various rubbers, anti-vibration agents for vehicles, compounding agents thereof, asphalt-based paints, etc. As compounding agents, electrical insulation materials, compounding agents thereof, etc.Furthermore, as combustion improvers for waste incinerators, soil conditioners for plant growth, soil conditioners for wetlands and soft ground, heat insulating agents, compounding agents thereof, etc. can also be used with excellent workability and ease of handling.
以下、実施例により、本発明の再溶融性アスフアルト粉
末製造の数態様について、更に具体的に例示する。Hereinafter, several embodiments of the production of remeltable asphalt powder of the present invention will be illustrated in more detail with reference to Examples.
実施例 1
プローンアスフアルト 100重量部に触媒と
してAt2(SO4)35重量部を加え230℃で1時
間攪拌加熱する。Example 1 35 parts by weight of At2(SO4) as a catalyst was added to 100 parts by weight of prune asphalt, and the mixture was stirred and heated at 230°C for 1 hour.
ここでアスフアルトは次第に粘度を上昇し粘稠液となる
。Here, the asphalt gradually increases its viscosity and becomes a viscous liquid.
これにポリエチレン粉末(軟化点128℃)5重量部を
加え、約20分間、溶融反応させる。5 parts by weight of polyethylene powder (softening point: 128°C) is added to this, and the mixture is melted and reacted for about 20 minutes.
これを冷却し粗砕ののち固定・・ンマ一式粉砕機で粉末
化し最小約0.1WIL径のアスフアルトの粉末を得た
。This was cooled, coarsely crushed, and then pulverized using a fixed mass crusher to obtain asphalt powder with a minimum diameter of about 0.1 WIL.
実施例 2
ストレートアスフアルト 100重量部に触媒と
して
P2O57重量部
を加えて230〜270℃で2時間攪拌加熱する。Example 2 57 parts by weight of P2O as a catalyst was added to 100 parts by weight of straight asphalt, and the mixture was stirred and heated at 230 to 270°C for 2 hours.
更にこれに
ポリエチレン粉末(軟化点 30重量部128℃
)
を加え20分間よく溶融するとこのアスフアルト物質は
極めて高い粘度の半固状物となる。Furthermore, polyethylene powder (softening point: 30 parts by weight, 128°C) is added to this.
) is added and melted well for 20 minutes, this asphalt material becomes a semi-solid substance with extremely high viscosity.
これを実施例1と同様冷却、粗砕し、粉末化するときは
最小約0.17!t/!!L径のアスフアルト粉末が得
られる。When this is cooled, coarsely crushed, and powdered as in Example 1, the minimum is about 0.17! T/! ! Asphalt powder of L diameter is obtained.
Claims (1)
を含有する溶融混合物を粉末化してなる再溶融性アスフ
ァルト粉末。 2 アスファルト類を触媒の存在下に強酸化処理し、得
られた強酸化処理アスファルト類とオレフィン系樹脂類
を含有する溶融混合物を形成し、冷却したのち粉末化処
理することを特徴とする再溶融性アスファルト粉末の製
法。[Scope of Claims] 1. Remeltable asphalt powder obtained by pulverizing a molten mixture containing strongly oxidized asphalt and olefin resins. 2 Remelting characterized by strongly oxidizing asphalt in the presence of a catalyst, forming a molten mixture containing the obtained strongly oxidized asphalt and olefin resins, cooling it, and then powdering it. Production method of asphalt powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP453580A JPS5912712B2 (en) | 1980-01-21 | 1980-01-21 | Remeltable asphalt powder and its manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP453580A JPS5912712B2 (en) | 1980-01-21 | 1980-01-21 | Remeltable asphalt powder and its manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56103280A JPS56103280A (en) | 1981-08-18 |
| JPS5912712B2 true JPS5912712B2 (en) | 1984-03-24 |
Family
ID=11586731
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP453580A Expired JPS5912712B2 (en) | 1980-01-21 | 1980-01-21 | Remeltable asphalt powder and its manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5912712B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6180111U (en) * | 1984-10-31 | 1986-05-28 | ||
| JPS63315853A (en) * | 1987-06-13 | 1988-12-23 | ダイムラー−ベンツ アクチエンゲゼルシヤフト | Louver type vent hole blasting air into automobile cabin |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5938281A (en) * | 1982-08-30 | 1984-03-02 | Fuji Standard Res Kk | Crushing of pitch and raw coke and crushed powder composition |
-
1980
- 1980-01-21 JP JP453580A patent/JPS5912712B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6180111U (en) * | 1984-10-31 | 1986-05-28 | ||
| JPS63315853A (en) * | 1987-06-13 | 1988-12-23 | ダイムラー−ベンツ アクチエンゲゼルシヤフト | Louver type vent hole blasting air into automobile cabin |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56103280A (en) | 1981-08-18 |
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