INVESTIGATION THE OLIGOMERIZATION PROCESS OF HEXENE-1

Shahla Alizade, I. Jamal, A. Ali, AliyevFariz Ramik
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Abstract

In article for oligomerization and alkylation processes, to obtain a useful and highly stable active catalyst, New Catalytic Complex (NCC) synthesized which is based on aluminum metal using C2H4Cl2 and this complex has shown high stability in alkylation, oligomerization processes compared to other aluminum-containing catalysts. It is difficult to regulate the molecular mass distribution of received products during oligomerization, either Intensificate the oligomerization process of olefins that is why this process take place in presence of obtaining of bimetal catalytic complex with a highly stable activity from the modification of the New Catalytic Complex(NCC) with transition metal chloride. Comparatively studied oligomerization of Hexen-1 in present of new bimetallic catalytic complex which was modified by NCC and chromium salt (NCC/CrCl3), effect of temperature, reaction time, concentration of the catalyst and the proportion of catalyst components (Al:Cr) in the process was investigated.It was determined that at the initial time (10 min) conversion hexene-1 and the yield of purposeful oil fraction were low. Increasing time, conversion rate of Hexen-1 increases and the optimal time for the process is considered as 60 minutes. In low concentrations of catalyst (0,1-0,3)  oligomerization of hexene-1 is low but in high concentrations(>1%) reaction goes with high rate, at optimal concentration 0,5% mass both the yield of oil fraction and its chemical-physical properties were high.In oligomerization process investigated  ratio effect of catalyst components Al: Cr that was used  Al: Cr=(4-32):1 mol.It has been revealed that oligomerization of Hexen-1, at low mol ratio of components (4:1), received yield of oligomer fraction decreases while mol ratio increases (16:1, 32:1).Studies determined that bimetallic complex at 8:1 mole has shown the maximal activity in  oligomerization process of Hexen-1.The effect of the temperature on the oligomerization process was studied in the range of 30-60oC, increasing the temperature up to 50 °C has a positive effect on the course of the process and despite providing complete oligomerization of hexene-1 its also providing increasing the amount of oil fractions with high viscosity. According to the researches, the optimal conditions for the oligomerization process of hexene-1 with the participation of the bimetallic catalytic complex: reaction time – 60 min., concentration of catalyst – 0,5 % by wt., mol ration of components Al:Cr = 8:1, temperature – 50 °C. In known optimal condition its possible to obtain oligomers with physical indications, characterized by narrow molecular mass distribution, by new catalytic complex that was modified by chromium salt.Such products have special importance, as low-freezing, high viscosity index qualitative engine oils.Synthesis of bimetallic catalytic complexes, with their presence in oligomerization of olefins and fractions, opens wide range perspectives in synthesis of different high-molecular compounds in industry
己烯-1寡聚过程的研究
本文针对低聚和烷基化过程,为获得一种有用的、高稳定的活性催化剂,以C2H4Cl2为原料合成了以铝为基材的新型催化配合物(NCC),该配合物在烷基化、低聚过程中表现出较其它含铝催化剂较高的稳定性。在低聚过程中很难调节接收产物的分子质量分布,要么加剧烯烃的低聚过程,这就是为什么这个过程发生在用过渡金属氯化物修饰新催化配合物(NCC)获得具有高度稳定活性的双金属催化配合物的情况下。比较研究了NCC和铬盐(NCC/CrCl3)改性的新型双金属催化配合物对己烯-1的寡聚反应,考察了温度、反应时间、催化剂浓度和催化剂组分(Al:Cr)比例对反应的影响。结果表明,在初始时间(10 min)转化己烯-1和目的油馏分的收率较低。随着时间的增加,Hexen-1的转化率增加,该过程的最佳时间为60分钟。在低浓度(0,1-0,3)催化剂下,己烯-1的低聚反应速率较低,而在高浓度(>1%)催化剂下,反应速率较高,在最佳浓度(0,5%质量)下,油馏分收率和理化性质均较高。在低聚过程中,采用Al: Cr=(4-32):1 mol,考察了催化剂组分Al: Cr的比例效应。结果表明,在低组分摩尔比(4:1)下,已烯-1的低聚反应,低组分摩尔比(16:1,32:1)越大,低聚产物收率越低。研究表明,在Hexen-1的寡聚过程中,8:1摩尔双金属配合物的活性最大。在30-60℃范围内研究了温度对低聚过程的影响,将温度提高到50℃对这一过程的进行有积极的影响,除了使己烯-1完全低聚外,还增加了高粘度油分的数量。根据研究,双金属催化配合物参与己烯-1寡聚反应的最佳条件为:反应时间- 60 min,催化剂质量分数- 0.5%,组分摩尔比Al:Cr = 8:1,反应温度- 50℃。在已知的最佳条件下,用铬盐修饰的新型催化配合物可以得到具有窄分子质量分布的物理表征的低聚物。这类产品具有特殊的重要性,如低凝固性、高粘度指数的定性发动机油。双金属催化配合物的合成,由于其在烯烃和馏分的低聚反应中的存在,为工业上不同高分子化合物的合成开辟了广阔的前景
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