氮辅助循环蒸汽增产的现场试验,以苏丹为例

Xueqing Tang, Chun-xu Yu, Yang Bai, Hui Lu, Mohamed Salaheldin Mohamed
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摘要

本文介绍了苏丹FNE油田Post-CHOPS井氮辅助循环蒸汽增产现场试验的关键方面。FNE油田是一种稠油资产,其成分梯度(API为13.87 ~ 18.1°,原位粘度为226 ~ 255 cp)位于深度为1500 ~ 1900英尺的块状松散砂岩中,渗透率为2 ~ 9达西,底部水驱力强。最初,稠油冷采砂(chop)被应用于整个区块上部的易采油。当CHOPS井的流量下降到经济极限,或者生产者温度过低(油藏温度111°F)而无法有效泵出时,氮气辅助循环蒸汽增产可以增加油藏压力,降低稠油粘度,并提高油井产量。具体技术要点如下:内部研究,包括粘度降低测试和数值模拟,建议以268bbl /ft为基础,以1260bbl /d的速率注入储层,每循环蒸汽量(冷水当量)为11442桶,质量为70%至75%,每循环注氮量为4.75 MMscf,浸泡时间为5至7天,使热量和压力在储层中分布更均匀,然后进入泡化过程。泵位于最底部射孔下方30-60英尺处,通过保持流体水平低于底部射孔,最大限度地提高流体产量。在泵送结束时,井底流动压力可降至70 psi。上倾井注汽、注氮顺序为先注蒸汽后注氮。对于下倾井,首先是注氮,然后是注蒸汽,以缓解水侵。再完井策略:将水泥挤进chop产层,因为这些产层含有虫孔,有些虫孔与含水层连通,然后在较低的产层段射孔,以提取粘性更高的稠油。生产套管失效风险评估:chop井采用热水泥对套管进行预张紧和全固井,进行后热作业。为了降低出砂风险,并且在初始生产时不会过度降低地层压力,初始返排流量被限制在500桶/天以下。在泵送过程中,所有流体沿着管柱向上开采,并将环空排出流管。泵以最佳速率工作,确保压降小于磨砂和水锥入的临界压降阈值。现场数据证实该试验是成功的,产量增加了2 - 3倍,含水率相对较低,没有出砂问题。对于类似稠油资产的后排骨井,该技术是一个有用的选择。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Field Trial of Nitrogen-Assisted Cyclic Steam Stimulation in Post-CHOPS Wells, Case Study in Sudan
This paper presents the key aspects of nitrogen-assisted cyclic steam stimulation field trial at Post-CHOPS wells in FNE field, Sudan. FNE field is a heavy-oil asset with compositional gradient (13.87 to 18.1°API, in-situ viscosity of 226 to 255 cp) in massive unconsolidated sandstones at depths of 1,500 to 1,900 ft, with a permeability of 2 to 9 Darcies and strong bottom-water drive. Initially, cold heavy oil production with sand (CHOPS) was applied to exploit easy oil at upper zones of entire play. When flow rates of CHOPS wells declined to economic limits, or producers were too cool (reservoir temperature 111°F) to pump efficiently, nitrogen-assisted cyclic steam stimulation was to increase reservoir pressure, decrease heavy-oil viscosity, and boost well production. The specific technical points are highlighted below: In-house studies, including viscosity reduction test and numerical simulations, recommended that steam volume (cold-water equivalent) of 11,442 bbl per cycle based on 268 bbl/ft, with 70 to 75% quality, will be injected into the reservoir at rate of 1,260 bbl/d, nitrogen injection volume per cycle is 4.75 MMscf, soak time is for 5 to 7 days to allow the heat and pressure to distribute more uniform through the reservoir, then go to puff process. Pump is set 30-60 ft below the lowermost perforations to maximize fluids production through keeping fluid-level well below bottom perforations. By the end of pumping, bottomhole flowing pressure can declined to 70 psi. Steam and nitrogen injection sequence at updip wells is to inject steam first, followed by nitrogen injection. For downdip wells, nitrogen injection is the first and steam injection comes later to mitigate water influx. Re-completion strategy: squeeze cement into CHOPS producing zones because they contain wormholes, some communicating with aquifer, and perforate the lower pay interval to extract more viscous heavy oil. Failure risk assessment of production casings: pre-tensioning and full cementing of the casing with thermal cement is adopted in CHOPS wells for post-CHOPS thermal operation. Initial flowback flow rate is limited to less than the level of 500 bbl/d to reduce sanding risk and does not unduly de-pressure the formation at initial production. During pumping process, all fluids are exploited up the tubing string and the annulus is vented the flow-line. Pump works at optimal rate to ensure pressure drawdown less than critical drawdown threshold for sanding and water coning. Field data confirmed that this trial is successful, with 2 to 3-fold production gain, relatively low water cut and no sanding issue. This technology is a useful option for post-CHOPS wells in the similar heavy-oil assets.
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