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process for the preparation of storm resistant resins

机译:制备耐候性树脂的方法

摘要

1349668 Production of aromatic petroleum hydrocarbon resins NIPPON OIL CO Ltd 21 July 1971 [22 July 1970] 34272/71 Heading C3P An aromatic hydrocarbon resin is produced by polymerizing at - 30‹ to 60‹ C. for 10 minutes to 15 hours in the presence of 0À01-5 wt. per cent of a Friedel Crafts catalyst and thereafter removing the catalyst, a fraction which has a conjugated diolefin content of 0À7 wt. per cent or less and the relationship wt. per cent of conjugated diolefin in fraction ¸ wt. per cent of polymerizable components in fraction Î 100 is 3% or less, a total content of indene and alkyl derivatives thereof of 2 wt. per cent or less and a relationship as above, but for indene of 8% or less, said fraction having been obtained by distillation from a hydrocarbon fraction having a B.Pt. range of 140-220‹ C. obtained by the thermal cracking of petroleum. Unreacted oil and low molecular weight polymer are also preferably removed from the product. The resin may be used in a paint composition which comprises (the parts being by wt. per 100 parts by wt. of the total composition) (1) 0-14 parts of a maleic acid resin, (2) 1-10 parts of a plasticizer, (3) 50-75 parts of pigment and/or filler, and (4) 24-49 parts of the aromatic hydrocarbon resin. Such paints are used especially for road markings. The invention also comprises a process for concurrently producing first and second aromatic hydrocarbon resins which comprises separating into fractions I and II by distillation, a hydrocarbon fraction of B.Pt. 140-220‹ C. obtained by the thermal cracking of petroleum, the separation being such that no intermediate fraction exists between said two fractions, the fraction being characterized in that fraction (I) is as defined for the fraction defined in the main invention above, and fraction (II) has a total content of indene and its alkyl derivatives of 20 wt. per cent or more and a relationship as defined above for indene, of 30% or more, and polymerizing separately said two fractions by the same method as described above, to prepare said first and second resins. The second resin finds use in printing ink compositions.
机译:1349668生产芳族石油烃树脂NIPPON OIL CO Ltd 1971年7月21日[1970年7月22日]标题C3P在存在的条件下,于-30℃至60℃聚合10分钟至15小时,可以生产芳族烃树脂。为0‑01-5重量。 %的Friedel Crafts催化剂,然后除去催化剂,其部分的共轭二烯烃含量为0-7wt%。百分比或更少和关系wt。分数¸wt。中共轭二烯烃的百分比分数α100中可聚合组分的百分比为3%或更少,茚及其烷基衍生物的总含量为2 wt。%。 %或更低,并且具有上述关系,但是对于8%或更低的茚,所述馏分是通过蒸馏从具有B.Pt的烃馏分中获得的。通过石油的热裂解获得140-220℃的温度范围。还优选从产物中除去未反应的油和低分子量聚合物。所述树脂可以用于涂料组合物中,所述涂料组合物包含(重量份占总组合物的每100重量份)(1)0-14重量份的马来酸树脂,(2)1-10重量份的马来酸树脂。增塑剂,(3)50-75份颜料和/或填料,和(4)24-49份芳烃树脂。这种涂料特别用于道路标记。本发明还包括同时生产第一和第二芳族烃树脂的方法,该方法包括通过蒸馏将B.Pt的烃馏分分离成馏分I和II。通过石油的热裂解获得140-220℃,分离使得在所述两个馏分之间不存在中间馏分,该馏分的特征在于馏分(I)如以上主要发明中定义的馏分所定义,馏分(II)的茚及其烷基衍生物的总含量为20重量%。 %或以上,以及如上对茚定义的关系为30%或以上,并通过与上述相同的方法分别聚合所述两个馏分,以制备所述第一和第二树脂。第二树脂可用于印刷油墨组合物中。

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