The Success Story of Optimization Gas Turbine Compressor and Generator Fuel Gas Pressure to Maximize Production in X Field

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Abstract

X plant with capacity 800 MMscfd has 2 major process plant, Inlet Compression system to lower the inlet pressure and gas plant to treat the raw gas to meet sales gas specification. The inlet compression consists of inlet cooling/separation and compression system. Currently, the inlet compression was operated with pressure 455, 420 and 400 psig at inlet header, separator, and suction compressor respectively. The condensate from separator flow to condensate stabilization system with pressure 380 psig. The flash gas in condensate system then used as fuel gas for gas turbine engine at 340 psig. There was a well drilling plan which require to shut-in one major well and lead to X production decrease to 670 MMscfd with inlet header pressure 455 psig. Reducing inlet header pressure couldn’t be done due to separator pressure requirement whereas allowing condensate can still flow to condensate system then become such a process bottleneck. Deep evaluation was performed to lower the fuel gas supply pressure of Turbines in purpose lower pressure in condensate system in term of gas hydrocarbon dewpoint, LHV, wobbe index, fuel gas valve opening, engine performance, acceleration time from light-off to idle speed, drop on speed/frequency during transient to maximum possible load. As study concluded, performance test was conducted and succeed to decrease the fuel gas supply pressure from 340 to 260 psig, then it is beneficial to reduce the inlet header pressure from 455 psig to as low as 375 psig. The optimization of HP fuel gas pressure can maximize production in X field from 670 MMscfd to 720 MMscfd with no additional capital cost during shut-in major well for new well drilling. Therefore, optimizing the fuel gas pressure of Gas turbine engine can maximize the well production.
优化燃气轮机压缩机和发电机燃气压力以实现X油田产量最大化的成功案例
产能800 MMscfd的X工厂有两个主要的工艺装置,入口压缩系统用于降低进口压力,气体装置用于处理原料气以满足销售气体规格。进气道压缩由进气道冷却/分离和压缩系统组成。目前,进口压缩分别在进口集管、分离器和吸气压缩机处的压力为455,420和400psig。凝结水从分离器流到凝结水稳定系统,压力为380psig。凝结水系统中的闪蒸气体在340 psig的压力下用作燃气轮机的燃气。有一个钻井计划要求关闭一口主要井,导致X产量下降到670 MMscfd,进口集管压力为455 psig。由于分离器压力的要求,降低进口集压无法实现,而允许凝结水仍然可以流到凝结水系统,这就成为了这样一个过程瓶颈。从燃气烃类露点、LHV、摆振指数、燃气阀开度、发动机性能、从点火到怠速加速时间、瞬态转速/频率降至最大可能负荷等方面对降低凝结水系统燃气供应压力进行了深入评估。研究结果表明,进行了性能测试,成功地将燃气供应压力从340 psig降低到260 psig,然后将进气总管压力从455 psig降低到375 psig。高压燃气压力的优化可以使X油田的产量从670万立方英尺/天提高到720万立方英尺/天,而在关井期间无需额外的投资成本。因此,优化燃气涡轮发动机的燃气压力可以最大限度地提高油井产量。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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