CN101358016B - 一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺 - Google Patents

一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺 Download PDF

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CN101358016B
CN101358016B CN2008101392160A CN200810139216A CN101358016B CN 101358016 B CN101358016 B CN 101358016B CN 2008101392160 A CN2008101392160 A CN 2008101392160A CN 200810139216 A CN200810139216 A CN 200810139216A CN 101358016 B CN101358016 B CN 101358016B
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逯大成
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Abstract

一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺,属于有机合成技术领域。以碳五树脂和碳九树脂为主要原料,其特征在于制备工艺按如下步骤依次进行:(1)以碳五树脂和碳九树脂为原料,在常压反应器中,控制反应温度为180℃—200℃,时间大于或等于2小时,生成脂肪类树脂——芳烃类树脂组成的混合物。(2)在上述体系中加入橡胶沥青,控制反应温度为180℃—200℃,时间大于或等于2小时,制得成品。本发明制备的石油树脂能改善不同极性及粘度橡胶的混合均匀性,缩短混炼时间,改善胶料流动性,提高胶料的定伸强度以及物理机械性能,从根本上克服了各类加工助剂对定伸强度降低的影响,撕裂强度上升、磨耗量下降。并且价格低廉,适于推广。

Description

一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺
技术领域
本发明属于有机合成技术领域,具体涉及一种石油树脂的制备工艺技术。 
背景技术
在轮胎工业中,对不同极性及粘度橡胶的混和普遍采用均匀剂。现有技术中普遍采用均匀剂40MSF应用于轮胎胎面胶。均匀剂40MSF是一种进口原料,目前国内尚无企业可以生产。均匀剂40MSF对缩短混炼时间、减低混炼能耗、改善炭黑分散效果、提高胶料混炼均匀性方面效果明显,但其缺点是价格较高。随着原材料价格的上涨,售价高昂的均匀剂40MSF对国内中小型企业显然负担太大。 
发明内容
本发明的目的在于提供一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺,通过该工艺制备的石油树脂,适用于不同橡胶、不同极性、不同粘度的橡胶混合物。 
本发明解决其技术问题采用的技术方案是:发明一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺,以碳五树脂和碳九树脂为主要原料,其特征在于制备工艺按如下步骤依次进行: 
(1)以碳五树脂和碳九树脂为原料,在常压反应器中,控制反应温度为180℃-200℃,时间大于或等于2小时,生成脂肪类树脂-芳烃类树脂组成的混合物。 
(2)在上述体系中加入橡胶沥青,控制反应温度为180℃-200℃,时间大于或等于2小时,制得成品。 
(3)各种原料消耗量为:碳五树脂8-10份,碳九树脂60-62份,橡胶沥青30-32份。 
本发明中,所述的碳五树脂为从轻油裂解制乙烯的副产液体分离出含有五个碳原子的烃的混合物经催化聚合反应而得。所述的碳九树脂为催化重整和裂解制乙烯副产的含九个碳原子的芳烃馏分经催化聚合反应而得。 
制备本发明的消耗原料的性能及要求: 
碳五树脂: 
Figure G2008101392160D00021
相对分子量500—2000。 
性状:碳五树脂为浅黄色固体,相对密度为0.71—1.07,软化点70—110℃,不溶于水、甲醇、乙醇,溶于丙酮、甲乙酮、醋酸乙酯、二氯乙烷、环已烷、苯、甲苯、溶剂汽油等。 
碳九树脂: 
结构式
Figure G2008101392160D00022
相对分子质量600—3000 
性状:碳九树脂为浅黄色至深琥珀色固体,相对密度0.970—0.975,软化点80—140℃,闪点260℃,不溶于水、甲醇、乙醇,溶于芳香烃和矿物油。 
橡胶沥青:以原油蒸馏所得的减压渣油经适当条件下的氧化而制的。 
性状:黑色固体,软化点125—135℃,针入度15—25,苯溶解度≥99.5%,闪点≥230℃,不溶于低沸点烷烃和丙酮、乙醚、稀乙醇,溶于二硫化碳、四氯化碳、吡啶等。 
本发明制备的石油树脂能改善不同极性及粘度橡胶的混合均匀性,缩短混炼时间,改善胶料流动性,改善在开炼、密炼机和压延机上的加工性能,提高胶料的定伸强度以及物理机械性能,从根本上克服了各类加工助剂对定伸强度降低的影响,撕裂强度上升、磨耗量下降。并且价格低廉,适于推广。 
具体实施方式
实施例一 
将碳五树脂10g、碳九树脂60g依次加入500ml烧瓶中,控制反应温度180℃,时间2 小时,在180℃,加入309橡胶沥青,均匀搅拌时间2小时后放料,得石油树脂40MSH产品,软化点95℃,灰分0.4%,外观呈黑褐色固体。 
实施例二 
将碳五树脂8g、碳九树脂62g依次加入500ml烧瓶中,控制反应温度190℃,时间2小时,在190℃,加入31g橡胶沥青,均匀搅拌时间2小时后放料,得石油树脂40MSH产品,软化点97℃,灰分0.5%,外观呈黑褐色固体。 
实施例三 
将碳五树脂9g、碳九树脂61g依次加入500ml烧瓶中,控制反应温度200℃,时间3小时,在200℃,加入32g橡胶沥青,均匀搅拌时间3小时后放料,得石油树脂40MSH产品,软化点96℃,灰分0.5%,外观呈黑褐色固体。

Claims (3)

1.一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺,以碳五树脂和碳九树脂为主要原料,其特征在于制备工艺按如下步骤依次进行:
(1)以碳五树脂和碳九树脂为原料,在常压反应器中,控制反应温度为180℃-200℃,时间大于或等于2小时,生成脂肪类树脂——芳烃类树脂组成的混合物;
(2)在上述体系中加入橡胶沥青,控制反应温度为180℃-200℃,时间大于或等于2小时,制得成品;
(3)各种原料消耗量为:碳五树脂8-10份,碳九树脂60-62份,橡胶沥青30-32份。
2.根据权利要求1所述的一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺,其特征在于所述的碳五树脂为从轻油裂解制乙烯的副产液体分离出含有五个碳原子的烃的混合物经催化聚合反应而得。
3.根据权利要求1所述的一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺,其特征在于所述的碳九树脂为催化重整和裂解制乙烯副产的含九个碳原子的芳烃馏分经催化聚合反应而得。
CN2008101392160A 2008-08-21 2008-08-21 一种以脂肪烃类树脂与芳烃类树脂混合制成石油树脂的制备工艺 Expired - Fee Related CN101358016B (zh)

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