首页> 外文期刊>Journal of the Japan Petroleum Institute >Thermal Cracking of Paraffinic and Middle East Atmospheric Residues and Hydrotreatment of Distillate Products
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Thermal Cracking of Paraffinic and Middle East Atmospheric Residues and Hydrotreatment of Distillate Products

机译:石蜡和中东常压渣油的热裂解和馏分油的加氢处理

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Thermal cracking of paraffinic atmospheric residue (AR) was performed in a continuous-flow reactor under the reaction conditions of 440-520 ℃ and N2 0.2-0.8 MPa, and the effects of the reaction temperature and pressure on the product distribution were examined. The vacuum residue fraction gradually decreased up to 480 ℃ and almost disappeared at higher temperatures. Accordingly, the yields of total distillate and coke increased and became nearly constant over 480 ℃. As the heavy distillate yield increased over 480 ℃, the yield of lighter distillates was the highest at 480 ℃ and decreased at higher temperature. When the reaction pressure was increased, the heavy distillate yield decreased with increasing yields of lighter distillates and coke. Two paraffinic and two Middle East ARs were thermally cracked under the conditions of 480 ℃, N2 0.4 MPa and 0.5 h, and the product composition and properties were compared. The yield of distillates (C4-500 ℃) was around 90 % for paraffinic ARs, and 70-80 % for Middle East ARs. The sulfur contents of the distillate products from paraffinic ARs were much lower than those of Middle East ARs, but the difference in the nitrogen contents was not significant. Pyrolyzed middle and heavy distillates were hydrotreated to investigate their hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) reactivities. The HDS rates of the distillates obtained from paraffinic ARs were 4-6 times higher than those of Middle East ARs. The HDN rates were comparable for the middle distillates, but the HDN rates of the heavy distillates from paraffinic ARs were lower than those from Middle East ARs.
机译:在连续流反应器中,在440-520℃和N2 0.2-0.8 MPa的反应条件下,对链烷烃常压渣油(AR)进行热裂解,并考察了反应温度和压力对产物分布的影响。真空残渣率在480℃时逐渐降低,在较高温度下几乎消失。因此,在480℃以上,总馏出物和焦炭的产率增加并几乎保持恒定。随着重馏出物产率在480℃以上的增加,较轻馏出物的产率在480℃时最高,而在较高温度下则降低。当反应压力增加时,重质馏出物产率随较轻质馏出物和焦炭的产率增加而降低。在480℃,N 2 0.4 MPa和0.5 h的条件下对两个石蜡族和两个中东AR进行了热裂解,并比较了产品的组成和性能。链烷烃ARs馏出物(C4-500℃)的产率约为90%,中东ARs馏出物的产率为70-80%。来自链烷烃ARs的馏出物产品的硫含量远低于中东ARs,但氮含量的差异不明显。对裂解的中,重质馏出物进行加氢处理,以研究其加氢脱硫(HDS)和加氢脱氮(HDN)反应性。从链烷烃ARs获得的馏出物的HDS速率比中东ARs高4-6倍。中级馏出物的HDN率是可比的,但链烷烃ARs的重馏分的HDN率低于中东ARs的HDN率。

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