二甲醚在稠油中扩散系数测定及其对蒸汽混注过程的影响
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    摘要:

    摘要:在“双碳”目标背景下,“高能耗、高碳排”稠油热采技术面临“提质增效和节能减排”双重挑战。将溶剂和蒸汽混合注入油藏可改善开发效果并极大降低能耗。二甲醚作为溶剂具有成本低、油水中都有一定溶解性等优势,具有巨大应用潜力。然而,二甲醚在原油中扩散系数这一决定传质过程的关键参数尚不明确。为此,本文以菲克第二定律、PR-EOS、二甲醚溶解度和混合黏度数据等为基础建立二甲醚扩散模型,结合高温高压下二甲醚压力衰减实验,通过模型网格化处理并逐层迭代各微元层的传质参数,对扩散系数经验关系式DAB = kTμ-β进行拟合,进而研究了二甲醚对混注过程的影响。研究结果表明:①扩散系数经验关系式拟合中优选β = 0.46,二甲醚在140 ℃和200 ℃下于油砂中的经验常数k分别为1.15×10-12和1.95×10-12;②高温高压下二甲醚在油样和油砂样中扩散系数的数量级为10-10 m2/s,升温会显著增大扩散系数,而多孔介质会减缓传质速率;③蒸汽二甲醚混注过程中二甲醚在泄油前缘的扩散深度为厘米级,据此可将前缘划分为温度和溶剂共同作用及温度为主的两个降黏区;④混注过程中二甲醚对泄油速度的贡献率约为11%,且原油黏度越高,二甲醚对泄油贡献率越高。本文建立了一套二甲醚扩散系数测定方法,具有成本低、速度快、结果可靠的优点,可准确量化特定温度下二甲醚在稠油中的扩散系数和浓度分布等,深化了对泄油前缘传质传热的机理认识,将为蒸汽二甲醚混注工艺应用提供指导。

    Abstract:

    To achieve carbon neutrality in the context of the 'Carbon Peaking and Carbon Neutrality' target, thermal recovery methods need to be improved. solvents and steam co-injection can improve the performance and greatly reduce energy consumption. As one promising solvent, Dimethyl ether (DME) has merits like low corrosiveness and certain solubility in both oil and water. However, the diffusion coefficient of DME in crude oil is still unclear. To this end, a diffusion model of DME was established based on the pressure-decay diffusion experiments at high temperature and high pressure, combined with Fick's second law, PR-EOS, solubility of DME and the mixture viscosity data, etc. By discretizing the entire model in which diffusion takes place into a number of control volumes, the parameters in each control volume were iterated one by one, and the empirical relationship of the diffusion coefficient, DAB = kTμ-β was fitted. After that, the effect of DME on the steam-solvent co-injection was analyzed. The results show that: (i) the empirical constant k of DME in oil sand at 140 ℃ and 200 ℃ are 1.15×10-12 and 1.95×10-12 respectively when β = 0.46 is used in fitting experimental data;(ii) the diffusion coefficient of DME in oil and oil sand at high temperature and high pressure range in the order of magnitude of 10-10 m2/s. Elevated temperature increases the diffusion coefficient while porous medium slows down the diffusion process. (iii) The diffusion depth of DME is several centimeters. So the drainage area would be divided into solvent diffusion-temperature dominated area and temperature dominated area;(iv) The contribution of DME to the oil production is about 11%, which is more significant for recovering high viscous reservoirs. In this paper, a set of low-cost and easy-to-implement method is established to calculate the diffusion coefficient of DME, which is confirmed to be reliable by fitting experimental data, and can accurately quantify the concentration distribution of DME in crude oil at a specific temperature, which deepens the mechanistic understanding of mass and heat transfer at drainage front, and provides theoretical guidance for the process of steam-solvent co-injection.

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  • 收稿日期:2024-08-20
  • 最后修改日期:2024-09-16
  • 录用日期:2024-09-17
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