Dimethyl Ether DME Solvent Based Enhanced-Oil-Recovery Technology - A Laboratory and Subsurface Study

H. Salimi, A. Ameri, J. Nieuwerf
{"title":"Dimethyl Ether DME Solvent Based Enhanced-Oil-Recovery Technology - A Laboratory and Subsurface Study","authors":"H. Salimi, A. Ameri, J. Nieuwerf","doi":"10.2118/200223-ms","DOIUrl":null,"url":null,"abstract":"\n DME as a water-soluble solvent for enhanced oil recovery has been introduced and some study results of DME enhanced waterflooding have recently been reported. However, DME-based EOR has not yet been implemented because of high prices of DME, the consequent need to recycle and reinject DME, and uncertain incremental oil per injected DME. This paper describes new insights into the different aspects (lab, subsurface, and economic) of DME-based EOR technology.\n An experimental protocol was defined to study the IFT, viscosity, and density of DME-Oil-brine mixtures as a function of T, P, and salinity, and DME compatibility with heavy components (e.g., asphaltenes), and adsorption on minerals.\n A compositional fractured-reservoir dynamic model that honors the PVT characteristics of DME was developed to investigate the performance of DME flood into fractured and unfractured reservoirs with light and heavy crudes.\n A business case as a function of DME recycling efficiencies, incremental oil, and phase implementation was discussed.\n The experimental results revealed that the oil viscosity 31 cP is significantly reduced to below 2 cP when mixed with DME in small volume ratios. No asphaltene precipitation (asphaltene content = 6.4 wt%) was observed when the oil was mixed with DME at increasing ratios up to 80 v/v%. Compatibility tests with formation water (total salinity 9.2 wt%) showed that DME is soluble in the formation water without any incompatibility or salting-out effect. The DME partitioning into oleic phase improves when temperature and brine-salinity increase. Imbibition tests at 5 bars and 50°C with DME-saturated formation water and limestone core plugs (permeability: 1.3–2.2 mD) increased the ultimate recovery to 70%.\n The simulation results indicate that DME injection into unfractured reservoirs does not improve the displacement efficiency, but it accelerates oil production because of improved injectivity up to 30%. However, DME injection into heavy-oil fractured reservoirs can improve displacement efficiency initially by enhancing imbibition rates from the matrix to the fracture system. However, this improved displacement efficiency decreases as DME injection continues because of DME breakthrough and there will be a point at which the DME displacement efficiency becomes the same as water. Nonetheless, DME significantly increases the recovery factor from heavy-oil fractured reservoirs (up to 200%).\n The economic results demonstrate that to have an economic DME-based EOR technology, the DME-recycling efficiency must be higher than 80%, incremental oil must be higher than 15%, and development must be a phased development plan.","PeriodicalId":10912,"journal":{"name":"Day 3 Wed, March 23, 2022","volume":null,"pages":null},"PeriodicalIF":0.0000,"publicationDate":"2022-03-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"1","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Day 3 Wed, March 23, 2022","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.2118/200223-ms","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 1

Abstract

DME as a water-soluble solvent for enhanced oil recovery has been introduced and some study results of DME enhanced waterflooding have recently been reported. However, DME-based EOR has not yet been implemented because of high prices of DME, the consequent need to recycle and reinject DME, and uncertain incremental oil per injected DME. This paper describes new insights into the different aspects (lab, subsurface, and economic) of DME-based EOR technology. An experimental protocol was defined to study the IFT, viscosity, and density of DME-Oil-brine mixtures as a function of T, P, and salinity, and DME compatibility with heavy components (e.g., asphaltenes), and adsorption on minerals. A compositional fractured-reservoir dynamic model that honors the PVT characteristics of DME was developed to investigate the performance of DME flood into fractured and unfractured reservoirs with light and heavy crudes. A business case as a function of DME recycling efficiencies, incremental oil, and phase implementation was discussed. The experimental results revealed that the oil viscosity 31 cP is significantly reduced to below 2 cP when mixed with DME in small volume ratios. No asphaltene precipitation (asphaltene content = 6.4 wt%) was observed when the oil was mixed with DME at increasing ratios up to 80 v/v%. Compatibility tests with formation water (total salinity 9.2 wt%) showed that DME is soluble in the formation water without any incompatibility or salting-out effect. The DME partitioning into oleic phase improves when temperature and brine-salinity increase. Imbibition tests at 5 bars and 50°C with DME-saturated formation water and limestone core plugs (permeability: 1.3–2.2 mD) increased the ultimate recovery to 70%. The simulation results indicate that DME injection into unfractured reservoirs does not improve the displacement efficiency, but it accelerates oil production because of improved injectivity up to 30%. However, DME injection into heavy-oil fractured reservoirs can improve displacement efficiency initially by enhancing imbibition rates from the matrix to the fracture system. However, this improved displacement efficiency decreases as DME injection continues because of DME breakthrough and there will be a point at which the DME displacement efficiency becomes the same as water. Nonetheless, DME significantly increases the recovery factor from heavy-oil fractured reservoirs (up to 200%). The economic results demonstrate that to have an economic DME-based EOR technology, the DME-recycling efficiency must be higher than 80%, incremental oil must be higher than 15%, and development must be a phased development plan.
查看原文
分享 分享
微信好友 朋友圈 QQ好友 复制链接
本刊更多论文
基于二甲醚二甲醚溶剂的提高采收率技术-实验室和地下研究
介绍了二甲醚作为提高采收率的水溶性溶剂,近年来也报道了一些二甲醚增强水驱的研究成果。然而,由于二甲醚的价格高,因此需要回收和重新注入二甲醚,并且每次注入二甲醚的石油增量不确定,因此尚未实施基于二甲醚的提高采收率。本文描述了基于dme的EOR技术在不同方面(实验室、地下和经济)的新见解。我们制定了一个实验方案来研究二甲醚-油-盐水混合物的IFT、粘度和密度随T、P和盐度的变化,以及二甲醚与重质组分(如沥青质)的相容性,以及对矿物的吸附。为了研究含轻质和重质原油的裂缝性和非裂缝性油藏中DME驱油的性能,建立了一个考虑DME PVT特征的裂缝性油藏组成动力学模型。一个商业案例作为二甲醚回收效率、增量油和阶段实施的函数进行了讨论。实验结果表明,当与二甲醚以小体积比混合时,油品粘度31 cP显著降低至2 cP以下。当油与二甲醚的混合比例增加到80 v/v%时,没有观察到沥青质沉淀(沥青质含量= 6.4 wt%)。与地层水的配伍性测试(总盐度为9.2 wt%)表明,二甲醚可溶于地层水,无不相容性和盐析作用。随着温度和盐盐浓度的升高,二甲醚向油相的分配有所改善。在5 bar和50°C条件下,采用饱和二甲苯的地层水和石灰岩岩心塞(渗透率:1.3-2.2 mD)进行渗吸试验,最终采收率提高到70%。模拟结果表明,在未裂缝油藏中注入二甲醚并没有提高驱替效率,但由于注入能力提高了30%,从而提高了采收率。然而,在稠油裂缝性油藏中注入二甲醚可以通过提高基质到裂缝系统的渗吸速率来提高驱替效率。然而,随着DME的继续注入,由于DME的突破,这种提高的驱替效率会下降,并且会有一个点,DME的驱替效率会变得和水一样。然而,DME显著提高了稠油裂缝性油藏的采收率(高达200%)。经济结果表明,要实现经济的dme提高采收率技术,dme回收效率必须高于80%,增量油必须高于15%,开发必须分阶段进行。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 去求助
来源期刊
自引率
0.00%
发文量
0
期刊最新文献
Sea-Fastening Analysis and Design of a Horizontally Transported Large Jacket Brownfield Waterflood Management - Strategic Implementation of Field Trial Learning, South Oman Interpretation of the Alkaline-Surfactant-Polymer Pilot in West Salym Using Tracers What is the Optimum Wettability for Oil Recovery Through Waterflooding? In-Situ Wettability Determination Using Magnetic Resonance Restricted Diffusion
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
现在去查看 取消
×
提示
确定
0
微信
客服QQ
Book学术公众号 扫码关注我们
反馈
×
意见反馈
请填写您的意见或建议
请填写您的手机或邮箱
已复制链接
已复制链接
快去分享给好友吧!
我知道了
×
扫码分享
扫码分享
Book学术官方微信
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术
文献互助 智能选刊 最新文献 互助须知 联系我们:info@booksci.cn
Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。
Copyright © 2023 Book学术 All rights reserved.
ghs 京公网安备 11010802042870号 京ICP备2023020795号-1