JPS6134751B2 - - Google Patents
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- JPS6134751B2 JPS6134751B2 JP16035877A JP16035877A JPS6134751B2 JP S6134751 B2 JPS6134751 B2 JP S6134751B2 JP 16035877 A JP16035877 A JP 16035877A JP 16035877 A JP16035877 A JP 16035877A JP S6134751 B2 JPS6134751 B2 JP S6134751B2
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- epoxy resin
- oil
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- weight
- epoxy
- 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.)
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- Compositions Of Macromolecular Compounds (AREA)
- Epoxy Resins (AREA)
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Description
本発明は耐油性、耐食性にすぐれたエポキシ系
の硬化性被覆組成物に関する。
従来から耐食性のすぐれたエポキシ系樹脂組成
物たとえば瀝青質エポキシ樹脂組成物は耐水性、
耐塩水性、耐油性などの特性を有しており船舶バ
ラストタンク、原油タンク、水道鋼管等の重防食
分野に広く用いられている。
とくに船舶のバラストタンクは原油と海水が交
互に入るため激しい腐食環境にあり、その重防食
材料としては高度の耐油性と耐海水性が要求さ
れ、また外観部分の被覆ではないため、比較的安
価で大量に供給され得るという理由で、黒色のこ
れら瀝青質エポキシ樹脂が用いられている。
瀝青質としてはコールタール系のものと石油系
のものがあり、一般にはコールタール系のものが
主に使用されている。これは石油系の代表的なも
のである。ストレートアスフアルト、ブローンア
スフアルトなどはエポキシ樹脂およびアミン系硬
化剤との相溶性が一般に悪くそのまま実用するこ
とは困難であるからである。
ところが、コールタール系のものは、塗布作業
を行なう者の健康をそこなう恐れがあると考えら
れており、このような環境衛生上の理由からコー
ルタール系に代わる安価ですぐれた被覆組成物が
広く求められている。
他方、これら被覆組成物は特にバラストタン
ク、原油タンクなどの塗布に用いられる場合には
鉱油類と接触するためすぐれた耐油性が要求され
る。すなわち塗布硬化後鉱油と接触した際に鉱油
中に抽出される被覆組成物の量がきわめて微少で
なければならない。
アスフアルト系エポキシ組成物については、後
記比較例で示すように耐油性が充分でない。
本発明はこれらの欠点を解決した耐食性、耐油
性にすぐれた新規なエポキシ系被覆組成物に関す
るものである。
本発明は、分子中に少なくとも2個以上のエポ
キシ基を有するエポキシ系樹脂100重量部、石油
系炭化水素の熱分解、水蒸気分解により得られる
沸点150℃以上の重質油を350ないし400℃の範囲
内の任意の温度において熱処理した石油系ピツチ
40〜200重量部、および適量のエポキシ系樹脂硬
化剤、を含む耐油性のすぐれた硬化性被覆組成物
を提供することを目的とする。
以下に本発明をさらに詳細に説明する。
本発明でいう石油系炭化水素は、原油、軽油、
灯油、ナフサなどのもので、通常これらを600〜
1000℃で熱分解又は水蒸気分解してエチレン、プ
ロピレンなどの低級オレフイン類を製造する際に
副生物として得られる重質油で、沸点150℃以上
のものが本発明の組成物の原料油として採用され
る。
本発明はこの原料油を350ないし400℃好ましく
は370〜390℃において熱処理させたものである。
この反応生成物を必要に応じて減圧蒸留して軽質
分を除去するかもしくは軽質油分をカツトパツク
することにより粘度を調整し、エポキシ樹脂との
混合性、作業性を調節することができる。
後記比較例で示すように反応温度は350℃未満
ではエポキシ樹脂との相溶性が悪く組成物の実用
強度が小さく耐油性も著しく悪くなる。また反応
温度が400℃を越すとエポキシ樹脂との相溶性が
悪くなる結果となる。
このように所定の温度範囲に熱処理した場合に
初めてすぐれた性状を示す理由は厳密には明らか
でない。しかしながら、350℃未満では熱処理に
よる重質油の熱重合、熱分解その他の複雑な反応
が充分進行しておらず、所望の性状を満足する物
質が生成されていないものと考えられ、また高温
となると、より高分子量化の反応などが進行しす
ぎて、やはり所望の性状の物質が生成されないも
のと考察される。
なお、コールタール系の場合については、前記
した欠点があるがコールタール中に多く含まれる
多環芳香族類(ベンゼン不溶分)又はフエノール
類が存在しているために耐油性が比較的に良いエ
ポキシ組成物となり、これに対してアスフアルト
系のものは脂肪族炭化水素が主成分であるために
エポキシ樹脂との相溶性が悪くなり、耐油性が不
良となると一般に考えられている。これらの一般
的な考察に反して、本発明で言う原料油の熱処理
物は通常ベンゼン不溶分は約10%以下であり多環
芳香族はきわめて少ないものであるが、すぐれた
耐油性を有するエポキシ組成物を与えるものであ
る。このように本発明で言う原料油を所定の温度
による熱処理をすることにより始めてすぐれたエ
ポキシ組成物が得られることはきわめて驚くべき
ことである。
熱処理は通常の反応器たとえば撹拌容器にまた
は管式反応器に該原料油を供給して加熱撹拌する
ことにより達成される。反応時間は特に限定はな
いが、通常10分ないし10時間好ましくは20分ない
し3時間である。
反応圧力も特に限定がないが通常大気圧または
加圧たとえば0〜50Kg/cm2Gで実施される。
反応はバツチ式または連続式で行なうことがで
きる。反応器に供給する前に予備加熱することは
もちろん可能である。
次に本発明においては、分子中に少なくともエ
ポキシ基
The present invention relates to an epoxy-based curable coating composition having excellent oil resistance and corrosion resistance. Traditionally, epoxy resin compositions with excellent corrosion resistance, such as bituminous epoxy resin compositions, have excellent water resistance,
It has characteristics such as salt water resistance and oil resistance, and is widely used in heavy corrosion protection fields such as ship ballast tanks, crude oil tanks, and steel water pipes. In particular, ships' ballast tanks are in a severely corrosive environment as crude oil and seawater enter alternately, and the heavy-duty anticorrosion materials required are highly resistant to oil and seawater, and are relatively inexpensive as they do not cover external parts. These black bituminous epoxy resins are used because they can be supplied in large quantities. There are two types of bituminous materials: coal tar-based ones and petroleum-based ones, and generally coal tar-based ones are mainly used. This is a typical petroleum-based product. This is because straight asphalt, blown asphalt, etc. generally have poor compatibility with epoxy resins and amine curing agents, making it difficult to put them to practical use as they are. However, coal tar-based coating compositions are thought to pose a risk to the health of those who apply them, and for environmental hygiene reasons, cheaper and better alternative coating compositions to coal tar-based coatings are widely sought after. It has been demanded. On the other hand, especially when these coating compositions are used for coating ballast tanks, crude oil tanks, etc., they are required to have excellent oil resistance since they come into contact with mineral oils. That is, the amount of the coating composition extracted into the mineral oil upon contact with the mineral oil after application and curing must be extremely small. Asphalt-based epoxy compositions do not have sufficient oil resistance, as shown in Comparative Examples below. The present invention relates to a novel epoxy coating composition that overcomes these drawbacks and has excellent corrosion resistance and oil resistance. The present invention uses 100 parts by weight of an epoxy resin having at least two epoxy groups in the molecule, heavy oil with a boiling point of 150°C or higher obtained by thermal decomposition of petroleum hydrocarbons, or steam decomposition at 350 to 400°C. Petroleum based pitch heat treated at any temperature within the range
The object of the present invention is to provide a curable coating composition having excellent oil resistance and containing 40 to 200 parts by weight and an appropriate amount of an epoxy resin curing agent. The present invention will be explained in more detail below. The petroleum hydrocarbons referred to in the present invention include crude oil, light oil,
Things such as kerosene and naphtha, which usually cost 600~
A heavy oil obtained as a by-product during the production of lower olefins such as ethylene and propylene by thermal decomposition or steam decomposition at 1000°C, with a boiling point of 150°C or higher, used as the raw material oil for the composition of the present invention. be done. In the present invention, this raw material oil is heat-treated at 350 to 400°C, preferably 370 to 390°C.
The viscosity of the reaction product can be adjusted by distilling the reaction product under reduced pressure to remove light components or by cutting off light oil components, and the miscibility with the epoxy resin and workability can be adjusted. As shown in the Comparative Examples below, if the reaction temperature is lower than 350°C, the composition will have poor compatibility with the epoxy resin, and the practical strength of the composition will be low, and the oil resistance will also be extremely poor. Moreover, if the reaction temperature exceeds 400°C, the compatibility with the epoxy resin will deteriorate. It is not exactly clear why excellent properties are exhibited only after heat treatment within a predetermined temperature range. However, it is thought that the thermal polymerization, thermal decomposition, and other complex reactions of heavy oil due to heat treatment do not proceed sufficiently at temperatures below 350°C, and a substance that satisfies the desired properties is not produced. In this case, it is considered that the reaction to increase the molecular weight progresses too much and a substance with the desired properties is not produced. In the case of coal tar, although it has the disadvantages mentioned above, it has relatively good oil resistance due to the presence of polycyclic aromatics (benzene insoluble matter) or phenols, which are contained in large amounts in coal tar. It is generally believed that asphalt-based compositions, on the other hand, have poor compatibility with epoxy resins and poor oil resistance because their main components are aliphatic hydrocarbons. Contrary to these general considerations, the heat-treated feedstock oil referred to in the present invention usually has a benzene insoluble content of about 10% or less and a very small amount of polycyclic aromatics, but it is an epoxy resin with excellent oil resistance. composition. It is quite surprising that an excellent epoxy composition can only be obtained by heat-treating the raw material oil at a predetermined temperature in the present invention. The heat treatment is accomplished by supplying the raw material oil to a conventional reactor, such as a stirring vessel or a tubular reactor, and heating and stirring it. The reaction time is not particularly limited, but is usually 10 minutes to 10 hours, preferably 20 minutes to 3 hours. The reaction pressure is also not particularly limited, but it is usually carried out at atmospheric pressure or a pressurized pressure of 0 to 50 kg/cm 2 G. The reaction can be carried out batchwise or continuously. It is of course possible to preheat it before feeding it to the reactor. Next, in the present invention, at least an epoxy group is added in the molecule.
【式】を2個以上有するエ
ポキシ系樹脂を一成分として用いる。これらの樹
脂はエポキシ基との結合部分が芳香族、複素環
式、脂肪族、環状脂肪族またはそれらの誘導体等
より構成されており、通常コールタール系、エポ
キシ樹脂に用いられているものと同じものであ
り、代表的には、グリシジル・エーテル型、グリ
シジル・エステル型、グリシジルアミン型などの
グリシジルエポキシ樹脂、エポキシ化オレフイン
型、エポキシ化植物油、環状脂肪族エポキシ樹脂
などの脂肪族エポキシ樹脂等が代表的なものであ
る。これらの具体例としてはエピクロールヒドリ
ンとビスフエノールAから生成されるエピ・ビス
型エポキシ樹脂、ポリプロピレングリコールジグ
リシジルエーテル、ペンタエリスリトールポリグ
リシジルエーテルなどである。
使用するエポキシ樹脂と前記熱処理重質油との
量は、エポキシ系樹脂100重量部に対して熱処理
重質油40ないし200重量部好ましくは50ないし150
重量部である。
さらに本発明の組成物は必須成分としてエポキ
シ樹脂硬化剤を含むものである。硬化剤は通常タ
ールエポキシ樹脂の硬化剤として使用されるもの
が用いられる。これらには脂肪族アミン、芳香族
アミン、アミンアダクト、酸無水物、ポリアミド
樹脂等でありたとえばジエチレントリアミン、ト
リエチレンテトラミン、テトラエチレンペンタミ
ン、N―アミノエチルピペラジン、イミダゾール
類、ピペリジン、ジエチルアミノプロピルアミ
ン、無水フタル酸、等である。
これら硬化剤の量は特に限定はないが、通常エ
ポキシ系樹脂100重量部に対して10〜150重量部用
いられる。なお、本発明の組成物は必須成分とし
て前記の三者を含むものであるがこれらのうちの
エポキシ系樹脂と硬化剤は塗布使用時に混合して
用いられるものである。熱処理重質油はエポキシ
系樹脂、硬化剤のいずれか又は双方にあらかじめ
混合しておくことができる。
本発明の組成物には、これら必須成分の他に通
常のエポキシ樹脂組成物に用いられる充てん剤、
稀釈剤、可撓性付与剤などを含むことができる。
以下に実施例をあげて本発明をさらに詳細に説
明する。
実施例 1
ナフサを水蒸気分解してオレフインを製造する
際に副生物として得られた沸点150℃以上の重質
残渣油を撹拌容器に収容し370℃において8Kg/
cm2の圧力下5時間反応せしめ、熱処理物を得た。
この熱処理物115部とエポキシ樹脂(シエル化学
社製エピコート828)100部、トリエチレンテトラ
ミン15部を混合して硬化物を得た。かかる硬化物
のトルエン抽出減量は7.2wt%であつた。なお硬
化物の耐油性の尺度とするトルエン抽出減量は
JIS K―6911―5.32に準拠して行なつた。すなわ
ち、混合直後の混合物を直径50mm、厚さ3mmに成
型して常温で7日間放置し、さらに温度50℃で1
日間養生し供試体とした。供試体を常温にてトル
エン中に入れ7日間後に取り出し、120℃、2時
間乾燥して、そのトルエンに抽出された減量を測
定した。
以下の実施例、比較例においても同様に測定し
た。これらの結果から、本発明のエポキシ樹脂組
成物はきわめて耐油性がすぐれていることが明ら
かである。
実施例 2
実施例1と同じ重質残渣油を原料として390℃
において10Kg/cm2の圧力下で1時間反応せしめ、
熱処理物を得た。これを用いて実施例1と同様の
配合により硬化物を得た。かかる硬化物のトルエ
ン抽出減量は4.5wt%であつた。
この結果は実施例1と同様に本発明のエポキシ
樹脂組成物がすぐれた耐油性を有することを示す
ものである。
実施例 3
実施例1と同じ重質油を撹拌容器に収容し、
390℃、9Kg/cm2、4時間熱処理する。得られた
処理物100部、エポキシ樹脂(三井石油化学エポ
キシ社製エポミツクR―139)100部、硬化剤とし
てジエチレントリアミンを12部添加して実施例と
同様に硬化させて、耐油性を測定した。トルエン
抽出量は7.0wt%であつた。
比較例 1
ストレートアスフアルト115部と実施例1のエ
ポキシ樹脂100部、トリエチレンテトラミン15部
を混合したが7日後でも充分な硬化物は得られ
ず、そのトルエン抽出減量は65wt%にも達し
た。
比較例 2
実施例1と同じ重質残渣油を原料として340℃
において5Kg/cm2の圧力下、1時間反応せしめ熱
処理物を得た。これを用いて実施例1と同様の配
合により硬化物を得た。かかる硬化物のトルエン
抽出減量は42.8wt%であつた。
比較例 3
実施例1と同じ重質残渣油を原料として420℃
において10Kg/cm2の圧力下で1時間反応せしめ熱
処理物を得た。これを用いて実施例1と同様の配
合により硬化物を得た。かかる硬化物のトルエン
抽出減量は42.8wt%であつた。
比較例 3
実施例1と同じ重質残渣油を原料として420℃
において10Kg/cm3の圧力下で1時間反応せしめ熱
処理物を得た。これを用いて実施例1と同様の配
合により硬化物を得た。かかる硬化物のトルエン
抽出減量は39.7wt%であつた。
比較例2および比較例3の結果は本発明で言う
特定の熱処理を行なわない場合にはすぐれた結果
を示さないことを表すものである。An epoxy resin having two or more of the following formula is used as one component. The bonding portion of these resins with the epoxy group is composed of aromatic, heterocyclic, aliphatic, cycloaliphatic, or derivatives thereof, and is usually the same as that used in coal tar-based and epoxy resins. Typical examples include glycidyl epoxy resins such as glycidyl ether type, glycidyl ester type, and glycidyl amine type, aliphatic epoxy resins such as epoxidized olefin type, epoxidized vegetable oil, and cycloaliphatic epoxy resin. It is representative. Specific examples of these include epi-bis type epoxy resin produced from epichlorohydrin and bisphenol A, polypropylene glycol diglycidyl ether, and pentaerythritol polyglycidyl ether. The amount of the epoxy resin and the heat-treated heavy oil used is 40 to 200 parts by weight of the heat-treated heavy oil, preferably 50 to 150 parts by weight, per 100 parts by weight of the epoxy resin.
Parts by weight. Furthermore, the composition of the present invention contains an epoxy resin curing agent as an essential component. As the curing agent, those commonly used as curing agents for tar epoxy resins are used. These include aliphatic amines, aromatic amines, amine adducts, acid anhydrides, polyamide resins, etc., such as diethylenetriamine, triethylenetetramine, tetraethylenepentamine, N-aminoethylpiperazine, imidazoles, piperidine, diethylaminopropylamine, phthalic anhydride, etc. Although the amount of these curing agents is not particularly limited, it is usually used in an amount of 10 to 150 parts by weight per 100 parts by weight of the epoxy resin. The composition of the present invention contains the above-mentioned three components as essential components, and among these, the epoxy resin and the curing agent are used as a mixture during coating. The heat-treated heavy oil can be mixed in advance with either or both of the epoxy resin and the curing agent. In addition to these essential components, the composition of the present invention includes fillers used in ordinary epoxy resin compositions,
A diluent, a flexibility imparting agent, etc. may be included. The present invention will be explained in more detail with reference to Examples below. Example 1 A heavy residual oil with a boiling point of 150°C or higher, obtained as a by-product when steam cracking naphtha to produce olefin, was stored in a stirring vessel, and at 370°C it was heated to 8 kg/kg.
The mixture was reacted for 5 hours under a pressure of cm 2 to obtain a heat-treated product.
A cured product was obtained by mixing 115 parts of this heat-treated product, 100 parts of an epoxy resin (Epicote 828 manufactured by Ciel Chemical Co., Ltd.), and 15 parts of triethylenetetramine. The toluene extraction loss of the cured product was 7.2 wt%. In addition, the toluene extraction loss, which is a measure of the oil resistance of the cured product, is
This was done in accordance with JIS K-6911-5.32. That is, the mixture immediately after mixing was molded into a diameter of 50 mm and a thickness of 3 mm, left at room temperature for 7 days, and further molded at a temperature of 50°C for 1 time.
It was cured for one day and used as a specimen. The specimen was placed in toluene at room temperature, taken out after 7 days, dried at 120°C for 2 hours, and the weight loss extracted by toluene was measured. Measurements were made in the same manner in the following Examples and Comparative Examples. From these results, it is clear that the epoxy resin composition of the present invention has extremely excellent oil resistance. Example 2 The same heavy residual oil as in Example 1 was used as a raw material at 390°C.
Reacted for 1 hour under a pressure of 10Kg/cm 2 at
A heat-treated product was obtained. Using this, a cured product was obtained by the same formulation as in Example 1. The toluene extraction loss of the cured product was 4.5 wt%. Similar to Example 1, this result shows that the epoxy resin composition of the present invention has excellent oil resistance. Example 3 The same heavy oil as in Example 1 was placed in a stirring container,
Heat treated at 390°C, 9Kg/cm 2 for 4 hours. 100 parts of the obtained treated product, 100 parts of epoxy resin (Epomiku R-139 manufactured by Mitsui Petrochemical Epoxy Co., Ltd.), and 12 parts of diethylenetriamine as a hardening agent were added, and the mixture was cured in the same manner as in the example, and the oil resistance was measured. The amount of toluene extracted was 7.0wt%. Comparative Example 1 115 parts of straight asphalt, 100 parts of the epoxy resin of Example 1, and 15 parts of triethylenetetramine were mixed, but a sufficiently cured product was not obtained even after 7 days, and the weight loss after extraction with toluene reached 65 wt%. Comparative Example 2 Using the same heavy residual oil as in Example 1 as a raw material, heating at 340℃
The mixture was reacted for 1 hour under a pressure of 5 kg/cm 2 to obtain a heat-treated product. Using this, a cured product was obtained by the same formulation as in Example 1. The toluene extraction loss of the cured product was 42.8 wt%. Comparative Example 3 The same heavy residual oil as in Example 1 was used as a raw material at 420°C.
A heat-treated product was obtained by reacting for 1 hour under a pressure of 10 kg/cm 2 . Using this, a cured product was obtained by the same formulation as in Example 1. The toluene extraction loss of the cured product was 42.8 wt%. Comparative Example 3 The same heavy residual oil as in Example 1 was used as a raw material at 420°C.
The mixture was reacted for 1 hour under a pressure of 10 kg/cm 3 to obtain a heat-treated product. Using this, a cured product was obtained by the same formulation as in Example 1. The toluene extraction loss of the cured product was 39.7 wt%. The results of Comparative Example 2 and Comparative Example 3 indicate that excellent results are not obtained when the specific heat treatment referred to in the present invention is not performed.
Claims (1)
有するエポキシ系樹脂100重量部、石油系炭化水
素の熱分解、水蒸気分解により得られる沸点150
℃以上の重質油を350ないし400℃の範囲内の任意
の温度において熱処理した石油系ピツチ40〜200
重量部、および適量のエポキシ系樹脂硬化剤を含
む耐油性硬化被覆組成物。 2 前記エポキシ系樹脂硬化剤がジエチレントリ
アミン、トリエチレンテトラミン、テトラエチレ
ンペンタミン、N―アミノエチルピペラジン、イ
ミダゾール類、ピペリジン、ジエチルアミノプロ
ピルアミン、無水フタル酸等であることを特徴と
する特許請求の範囲第1項記載の耐油性硬化被覆
組成物。 3 前記エポキシ系樹脂硬化剤をエポキシ系樹脂
100重量部に対し10〜150重量部含むことを特徴と
する特許請求の範囲第1項または第2項記載の耐
油性硬化被覆組成物。[Claims] 1. 100 parts by weight of an epoxy resin having at least two or more epoxy groups in the molecule, a boiling point of 150 obtained by thermal decomposition or steam decomposition of petroleum hydrocarbons.
Petroleum-based pitch 40-200 made by heat-treating heavy oil above ℃ at any temperature within the range of 350 to 400℃
parts by weight, and an appropriate amount of an epoxy resin curing agent. 2. Claim No. 2, characterized in that the epoxy resin curing agent is diethylenetriamine, triethylenetetramine, tetraethylenepentamine, N-aminoethylpiperazine, imidazoles, piperidine, diethylaminopropylamine, phthalic anhydride, etc. The oil-resistant cured coating composition according to item 1. 3 Adding the epoxy resin curing agent to the epoxy resin
The oil-resistant cured coating composition according to claim 1 or 2, which contains 10 to 150 parts by weight per 100 parts by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16035877A JPS5493022A (en) | 1977-12-30 | 1977-12-30 | Curable coating composition having oil resistance |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16035877A JPS5493022A (en) | 1977-12-30 | 1977-12-30 | Curable coating composition having oil resistance |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5493022A JPS5493022A (en) | 1979-07-23 |
| JPS6134751B2 true JPS6134751B2 (en) | 1986-08-09 |
Family
ID=15713238
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16035877A Granted JPS5493022A (en) | 1977-12-30 | 1977-12-30 | Curable coating composition having oil resistance |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5493022A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5411461B2 (en) * | 2008-07-03 | 2014-02-12 | 日鉄住金防蝕株式会社 | Corrosion preventive material for coating inner surface of corrosive fuel gas and anticorrosion method using the same |
| CN103725164B (en) * | 2013-12-03 | 2016-08-17 | 中国海洋石油总公司 | A kind of Raw oil-resistant coating composition |
-
1977
- 1977-12-30 JP JP16035877A patent/JPS5493022A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5493022A (en) | 1979-07-23 |
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