张大同, 滕霖, 李玉星, 叶晓, 顾帅威, 王财林. 管输CO2含水率计算方法[J]. 油气储运, 2018, 37(12): 1363-1367. DOI: 10.6047/j.issn.1000-8241.2018.12.007
引用本文: 张大同, 滕霖, 李玉星, 叶晓, 顾帅威, 王财林. 管输CO2含水率计算方法[J]. 油气储运, 2018, 37(12): 1363-1367. DOI: 10.6047/j.issn.1000-8241.2018.12.007
ZHANG Datong, TENG Lin, LI Yuxing, YE Xiao, GU Shuaiwei, WANG Cailin. Calculation methods for water content of pipeline CO2[J]. Oil & Gas Storage and Transportation, 2018, 37(12): 1363-1367. DOI: 10.6047/j.issn.1000-8241.2018.12.007
Citation: ZHANG Datong, TENG Lin, LI Yuxing, YE Xiao, GU Shuaiwei, WANG Cailin. Calculation methods for water content of pipeline CO2[J]. Oil & Gas Storage and Transportation, 2018, 37(12): 1363-1367. DOI: 10.6047/j.issn.1000-8241.2018.12.007

管输CO2含水率计算方法

Calculation methods for water content of pipeline CO2

  • 摘要: 管输CO2过程中,含水率是影响管道腐蚀速度的重要指标,为确保管道的安全运行,必须准确计算CO2的含水率。提出了两种含水率计算方法,分别为简化的热力学模型法和实验数据拟合的经验公式法。简化的热力学模型法利用PR(Peng-Robinson)状态方程计算相关物性参数,采用ϕ-γ方法对CO2-H2O两相体系进行描述;实验数据拟合的经验公式法采用现有的实验数据,拟合气态和超临界态管输CO2含水率计算经验公式。与文献的实测结果进行对比验证,管输条件下两种方法的计算精确度平均误差分别为1.40%和6.69%,均满足工程计算要求。根据误差分析结果,分别给出了两种方法的适用范围,研究成果对管输CO2管道的运行管理及其上游处理工艺的设计具有重要意义。

     

    Abstract: In the process of CO2 pipeline transportation, water content is an important factor affecting the corrosion rate of the pipelines. In order to ensure safe operation of pipelines, therefore, water content of CO2 shall be calculated accurately. In this paper, two different methods for calculating the water content of pipeline CO2 were put forward, i.e., the simplified thermodynamic model and the empirical formula based on experimental data fitting. In the simplified thermodynamic model, the related physical parameters are calculated by the Peng-Robinson state equation and the CO2-H2O two-phase system is described by means of ϕ -γ method. And in the empirical formula method based on experimental data fitting, the empirical formulas for calculating the water content of pipeline CO2 in gaseous and supercritical states are fitted with existing experimental data. It is verified by comparing with the actual measurement data in the existing literatures that average errors of calculation accuracy of the two methods under the condition of pipeline transportation are 1.40% and 6.69%, respectively, so both methods can satisfy the engineering calculation requirements. Finally, the application scope of two methods was proposed based on the error analysis results. The research results are of great significance for the operation management of pipeline CO2 and the design of upstream treatment process.

     

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