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Impact of Reservoir Mixing on Recovery in Enriched-Gas Drives Above the Minimum Miscibility Enrichment

机译:高于最小混溶度富集的储层混合对富气驱采收率的影响

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Gas enrichment is an important variable to optimize oilrecovery in enriched-gas drives. For slimtube experiments, oilrecoveries do not increase significantly with enrichmentsgreater than the MME. For field projects, however, theoptimum enrichment may be different from the MME. Theoptimum enrichment is likely the result of greater mixing inreservoirs than in slimtubes. In addition, 2-D effects such aschanneling, gravity tonguing, and crossflow can impact theenrichment selected.Numerical simulation is often used to model the effect ofphysical mixing on oil recovery in miscible-gas floods.Unfortunately, numerical dispersion can cloud theinterpretation of the results by artificially increasing the levelof mixing in the reservoir.This paper investigates the interplay between variousmixing mechanisms, enrichment level, and numericaldispersion. The mixing mechanisms examined are mechanicaldispersion, gravity crossflow, and viscous crossflow.UTCOMP is used to evaluate the effect of these mechanismson recovery for different grid refinements, reservoirheterogeneities, injection boundary conditions, relativepermeabilities, and numerical weighting methods includinghigher-order methods. For all simulations, the reservoir fluidused is a twelve-component oil displaced by gases enrichedabove the MME.The results show that for 1-D enriched-gas floods, therecovery difference for enrichments above the MMEincreases significantly with dispersion. The trend, however, isnot monotonic and shows a maximum at a dispersivity ofabout 3 ft. Furthermore, the trend is independent of relativepermeabilities and gas trapping for dispersivities less thanabout 3 ft, i.e. range of possible reservoir dispersivities. For 2-D enriched gas floods with slug injection, the difference inrecovery generally increases as dispersion and crossflowincrease. The magnitude of the recovery differences is lessthan for the 1-D displacements. Recovery differences for 2-Dare highly dependent on relative permeabilities and gastrapping. For water alternating gas (WAG) injection, thedifferences in recovery increase slightly with as dispersiondecreases. That is, the recovery difference is significantlygreater with WAG at low levels of dispersion than with sluginjection. For the cases examined, the magnitude of recoverydifference varies from about 1 to 8 percent of the original oilin-place (OOIP).
机译:气体富集是优化石油的重要变量 富气驱动器的恢复。对于薄管实验,油 浓缩不会使回收率显着增加 大于MME。但是,对于实地项目, 最佳富集可能与MME不同。这 最佳的富集可能是由于更大的混合比例 水库比在slimtubes。此外,二维效果例如 窜流,重力舌穿和横流都会影响 丰富选择。 数值模拟通常用于建模效果 在混溶性天然气驱中对采油进行物理混合。 不幸的是,数值分散会遮盖 通过人为地提高水平来解释结果 在储层中混合。 本文研究了各种因素之间的相互作用 混合机制,富集水平和数值 分散。检查的混合机制是机械的 分散,重力错流和粘性错流。 UTCOMP用于评估这些机制的效果 不同网格细化,油藏的采收率 异质性,注入边界条件,相对 磁导率和数值加权方法,包括 高阶方法。对于所有模拟,油藏流体 使用的是由富集气体置换的十二种成分的油 在MME之上。 结果表明,对于一维富集天然气驱, 超过MME的浓缩的采收率差异 随着色散显着增加。然而,趋势是 不是单调的,并且在分散度为时显示最大值 大约3英尺。此外,趋势与相对 渗透率和气体捕集的分散度小于 大约3英尺,即可能的储层分散度范围。对于2- D注入段塞的富集气驱,其区别在于 随着分散和错流,回收率通常会增加 增加。回收差异的幅度较小 而不是一维位移。二维恢复差异 高度依赖于相对渗透率和气体 诱捕。对于水交替气(WAG)注入, 随着分散,回收率差异略有增加 减少。即,恢复差异显着 在低分散度条件下,使用WAG时比使用团状时更大 注射。对于检查的病例,恢复的幅度 差异约为原始油的1%至8% 地点(OOIP)。

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