Converting of Waste Crude Oil of East Baghdad Oil Field into Light Hydrocarbons Using Thermal Cracking Technology

S. I. Hammoodi, K. A. Sukkar, Abdulridha H. Almajidi, Riyadh Almukhtar
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Abstract

East Baghdad oil field produces a lot of quantities of waste crude oil due to drilling and production processes activities. This waste is caused a negative impact on the environment and human health. In the present investigation, the collected waste crude oil of API= 13 was converted into light hydrocarbons via a thermal cracking reaction. The thermal cracking process was achieved in a batch reactor at temperatures ranging between 350-450°C in absence of oxygen. At each temperature, the reaction pressures varied between (1-6) kg/cm2. Moreover, a continuous stirring of the reaction mixture inside the reactor was continued during the course of the thermal cracking process at a velocity of 96 rpm. The best yield of produced liquid hydrocarbon, gases, and coke at optimum conditions was 77.56 wt.%, 9.3 wt.%, and 13.14 wt.%, respectively. Actually, this process regards cheap, and simple with a high rate of liquid hydrocarbon production as well as environmentally beneficial.
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利用热裂解技术将巴格达东部油田的废原油转化为轻烃
东巴格达油田在钻探和生产过程中会产生大量废弃原油。这些废物对环境和人类健康造成了负面影响。在本次调查中,收集到的 API= 13 的废原油通过热裂解反应转化为轻烃。热裂解过程在间歇式反应器中进行,温度在 350-450°C 之间,无氧。在每个温度下,反应压力在 (1-6) kg/cm2 之间变化。此外,在热裂解过程中,反应器内的反应混合物以每分钟 96 转的速度持续搅拌。在最佳条件下,生产的液态碳氢化合物、气体和焦炭的最佳产量分别为 77.56 重量百分比、9.3 重量百分比和 13.14 重量百分比。实际上,该工艺成本低廉,操作简单,液态碳氢化合物产量高,而且对环境有益。
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