Evaluation of the influence of hydrodynamic cavitation treatment of dark petroleum products on the yield of fractions with boiling points up to 400°C

B. V. Peshnev, E. V. Burlyaeva, V. B. Terenteva, D. Nikishin, A. Nikolaev, K. Andronov
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Abstract

Objectives. The reduction of the anthropogenic burden on the environment is generally associated with the transition to alternative energy sources. However, some of these have only regional significance, while the effectiveness of others remains doubtful. On this point, innovative processes aimed at increasing the depth of oil refining may be equally important for reducing the carbon footprint. Wave-based technologies such as cavitation may also be included in these processes. Among the various methods for inducing such cavitation phenomena in oil refining, hydrodynamic approaches are especially promising. It has been shown that the treatment effectiveness increases with greater pressure or when augmenting the number of cavitation processing cycles. The aim of this work is to identify the factor (i.e., pressure gradient or number of treatment cycles) having the greatest influence on the change of the characteristics of the oil product.Methods. Cavitation phenomena were created by pumping dark oil products through a diffuser. The pressure gradient ranged from 20 to 50 MPa, while the number of cavitation processing cycles varied from 1 to 10. The influence of cavitation conditions on the change of fractional composition of petroleum products was analyzed. Target fractions are those having a boiling point up to 400°C.Results. It is shown that increased pressure generated in the diffuser leads to a linear increase in the yield of desired cuts. The dependence of the yield of these fractions on the number of processing cycles is described by the growth model with saturation. A proposed equation describes the influence of pressure and number of cycles on the yield of the fractions from initial boiling point temperature (TIBP) to 400°C following cavitation processing of dark oil products. Some of the coefficients of this equation have been associated with the physicochemical characteristics of the feedstock.Conclusions. An equation for predicting the maximum possible yield of the TJBP-400°C fraction as a result of cavitation processing under different conditions of the process is proposed according to the physicochemical characteristics of the feedstock. The prediction error did not exceed 12%. The equation analysis and comparison of energy consumption between different process regimes shows that a higher yield of the target product is achieved by increasing pressure gradient rather than the number of processing cycles.
深色石油产品流体动力空化处理对沸点高达400℃馏分产率影响的评价
目标。减少人为对环境造成的负担通常与向替代能源的过渡有关。然而,其中一些措施仅具有区域意义,而其他措施的有效性仍令人怀疑。在这一点上,旨在增加炼油深度的创新工艺对于减少碳足迹可能同样重要。诸如空化等基于波浪的技术也可能包括在这些过程中。在炼油过程中诱导这种空化现象的各种方法中,水动力方法尤其有前景。研究表明,随着压力的增大或空化处理循环次数的增加,处理效果会增加。这项工作的目的是确定对油品特性变化影响最大的因素(即压力梯度或处理循环次数)。空化现象是由泵送深油产品通过扩散器产生的。压力梯度为20 ~ 50 MPa,空化处理次数为1 ~ 10次。分析了气蚀条件对石油产品馏分组成变化的影响。目标馏分是沸点高达400°c的馏分。结果表明,在扩散器中产生的压力增加导致所需切割的成品率线性增加。这些馏分的产率与加工循环次数的关系用饱和生长模型来描述。提出了一个方程,描述了压力和循环次数对黑油产品空化处理后从初始沸点温度(TIBP)到400°C馏分收率的影响。该方程的一些系数与原料的物理化学特性有关。根据原料的物理化学特性,提出了在不同工艺条件下空化处理TJBP-400°C馏分的最大可能产率的预测公式。预测误差不超过12%。通过方程分析和不同工艺条件下的能耗比较表明,提高压力梯度比增加加工循环次数更有利于提高目标产品的收率。
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