高粘度含水油的焦化

A. Nikolaev, B. V. Peshnev, E. V. Egorova
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摘要

目标。石油生产的一个特征是高粘度沥青油体积的增加。在俄罗斯,基于使用水蒸气的技术被用于提取它们。这种技术的使用会导致生产井的产品流中出现大量的水。用于加工的油的制备涉及其稳定、脱盐和脱水。由于萃取油的密度和含水的密度相当,传统的高粘度沥青油制备方案是无效的。解决这类油在燃料、能源和石油化学平衡中的问题的一个可能的办法是在其加工的第一阶段使用焦化过程。通过研究高粘度含水油焦化工艺条件对产物收率和特性的影响,可以达到这一目的。在实验室装置的“立方体”中进行了密度为1.0200 g/cm3的油的焦化,温度为50°C,含水量为18%。一个空心的圆柱形装置被用作反应器,并被放置在炉中。反应器内温度维持在500 ~ 700℃,压力维持在0.10 ~ 0.35 MPa。焦化过程温度的升高导致气态产物的数量增加,产生的焦炭数量减少,液体产物的数量对温度的依赖性更高,最大产量在550-600℃。工艺温度也影响液体产品的组成。在较低的温度下,液体产品中汽油和煤油馏分的含量较高。随着压力的增加,液态产物中气态产物、焦炭和低分子量烃馏分的数量也会增加。焦化过程中产生的焦炭的特性与商业生产的等级相似。值得注意的是,当炼焦含水的油时,高达98%的乳化液水随液体产品而去,其余的水留在形成的焦炭中。结果表明,焦化工艺在加工高粘度沥青油的初始阶段具有一定的应用前景。在这种情况下,由于延迟焦化技术方案允许汽油馏分与水分离,因此脱水阶段大大简化。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Coking of high-viscosity water-containing oil
Objectives. A characteristic feature of oil production is an increase in the volume of highviscosity bituminous oil. In Russia, technologies based on the use of water vapor are used for their extraction. The use of such technologies leads to a large amount of water in the product stream from the production well. Preparation of oil for processing involves its stabilization, desalination, and dewatering. Since the densities of the extracted oil and the water contained in it are comparable, traditional preparation schemes for processing of high-viscosity bituminous oil are ineffective. One of the possible solutions to the problem involving such oil in the fuel, energy, and petrochemical balance is to use a coking process at the first stage of its processing. This aim can be achieved by studying the influence of the process conditions of coking high-viscosity water-containing oil on the yield and characteristics of the resulting products.Methods. Coking of oil with a density of 1.0200 g/cm3 at 50 °C and with 18 wt % water content was carried out in a laboratory installation in a “cube.” A hollow cylindrical apparatus was used as a reactor and was placed in a furnace. The temperature and pressure in the reactor were maintained at 500–700 °C and 0.10–0.35 MPa, respectively.Results. An increase in the coking process temperature results in an increase in the amount of gaseous products, a decrease in the amount of the coke generated, and a higher dependence of the amount of liquid products on temperature with a maximum yield at 550–600 °C. The process temperature also affects the composition of liquid products. At a lower temperature, the amount of gasoline and kerosene fractions in liquid products is higher. With an increase in pressure, a higher amount of gaseous products, coke, and low-molecular-weight hydrocarbon fractions in liquid products could also be obtained. The characteristics of the coke produced in the coking process are similar to those of commercially produced grades. It is noted that when coking water-containing oil, up to 98% of the emulsion water goes with liquid products, and the remaining amount of water remains in the formed coke.Conclusions. Results showed the possible application of the coking process at the initial stage of processing high-viscosity bituminous oil. In this case, the dewatering stage is significantly simplified since the technological scheme of delayed coking allows the separation of the gasoline fraction from water.  
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