低温气体处理系统的建模

M. P. Kuznetsov
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When the pressure on the throttle decreases by every 0.4 MPa, the condensate output increases, if the pressure drops below 1.8 MPa, the specific condensate output will begin to decrease, which is explained by the pressure drop below the maximum condensation line of the phase diagram. The change in gas flow within the design values did not affect the operation of low-temperature separation. At any available low temperature and high pressure at the inlet to the ILTS, the most optimal mode will be when the pressure after the throttle is maintained within 1.8 - 1.9 MPa. The maximum specific yield of gas condensate (48.21%) was obtained at a pressure at the inlet to the ILTS of 5.1 MPa, a temperature after the heat exchanger of minus 2 o C and a pressure drop at the throttle of 3.05 MPa. 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引用次数: 0

摘要

目标。本工作的主要目的是:研究工艺参数变化对分离过程效率的影响,确定气田X碳纳米管在分离过程中的最佳工艺操作模式。方法。在KBC Petro-SIM计算机程序中解决了这一问题,并建立了LTS模型。为了进行这项研究,在KBC Petro-SIM计算机程序中建立了LTS的模型。结果。结果表明:在其他技术指标相同的情况下,在当前气体组成温度每降低2℃的情况下,比凝析油产率在15 ~ 30%的范围内增加,且温度越低,该百分比越高。当节流阀上的压力每降低0.4 MPa时,冷凝液的输出量增加,当压力降至1.8 MPa以下时,冷凝液的比输出量开始减少,这可以用相图中压力降至最大冷凝线以下来解释。气体流量在设计值范围内的变化对低温分离的运行没有影响。在任何可能的ILTS入口低温高压条件下,节流后压力保持在1.8 - 1.9 MPa为最佳模式。当进气压力为5.1 MPa,换热器后温度为- 2℃,节流压降为3.05 MPa时,凝析气比产率最高,为48.21%。作为数值研究的一部分,得到了以下结果:随着ILTC进口压力的增加,凝析气的比输出变化微不足道,但有了这个参数,可能会在节流阀上产生较大的压降;随着换热器出口气体温度的降低,冷凝气体的比产率增大;随着节气门压降的增大,凝析气的比输出增大,直到节气门后的压力达到1.8 ~ 1.9 MPa的范围。在这个区间内,达到了最大的比凝析油产量。随着节流阀上压降的进一步增大,凝析油的比输出减小。这可以用逆行冷凝现象来解释,因为最大冷凝线在这些压力范围内。结论。根据工作结果,发现开发的软件模块可以用于解决新出现的一系列问题。工作结果表明,所提出的方法适用于实际目的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Modeling of a low-temperature gas treatment system
Objective . The main purpose of the work is: investigation of the effect of changes in technological parameters on the efficiency of the separation process and determination of optimal technological modes of operation of gas field X CNTS in the separation process. Method . The problem was solved in the KBC Petro-SIM computer program and the LTS model was built. To conduct the study, a model of the LTS was built in the KBC Petro-SIM computer program. Result . The results obtained with the help of it showed: with the current composition of the gas with a decrease in temperature for every 2 o C, with other technological indicators being equal, the specific condensate yield increases in the range from 15 to 30%, and the lower the temperature, the higher this percentage. When the pressure on the throttle decreases by every 0.4 MPa, the condensate output increases, if the pressure drops below 1.8 MPa, the specific condensate output will begin to decrease, which is explained by the pressure drop below the maximum condensation line of the phase diagram. The change in gas flow within the design values did not affect the operation of low-temperature separation. At any available low temperature and high pressure at the inlet to the ILTS, the most optimal mode will be when the pressure after the throttle is maintained within 1.8 - 1.9 MPa. The maximum specific yield of gas condensate (48.21%) was obtained at a pressure at the inlet to the ILTS of 5.1 MPa, a temperature after the heat exchanger of minus 2 o C and a pressure drop at the throttle of 3.05 MPa. As part of the numerical research, the following results were obtained: with an increase in the pressure at the inlet to the ILTC, the change in the specific output of the gas condensate is insignificant, but with this parameter it is possible to create a larger pressure drop on the throttle; with a decrease in the gas temperature at the outlet of the heat exchanger, the specific yield of the gas condensate will increase; with an increase in the pressure drop at the throttle, the specific output of the gas condensate increases until the pressure after the throttle reaches the range of values of 1.8 – 1.9 MPa. In this interval, the maximum specific condensate yield is achieved. With a further increase in the pressure drop on the throttle, the specific output of the gas condensate decreases. This is explained by the phenomenon of retrograde condensation, since the maximum condensation line is in the range of these pressures. Conclusion . Based on the results of the work, it was found that the developed software module can be used to solve the emerging series of problems. The results of the work show the suitability of the proposed method for practical purposes.
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