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孤岛采油厂二〇一七年五月化学驱优化注入提质增效的主要做法孤东采油厂目录三、效果评价二、化学驱提质增效主要做法孤岛采油厂一、前言孤岛采油厂地质储量5.05亿吨,管理着孤岛、垦利等6个油田,形成了常规水驱、化学驱、稠油热采三种开发方式。孤岛油田储层物性好、高孔、高渗,非均质性强。孤岛地区勘探部署图三合村油田地质储量5.05亿吨化学驱稠油热采开发方式常规水驱孤岛油田构造井位图孤岛油田Ng5层粘度分布图地质储量4.11亿吨孤岛采油厂地质储量5.05亿吨,管理着孤岛、垦利等6个油田,形成了常规水驱、化学驱、稠油热采三种开发方式。孤岛油田储层物性好、高孔、高渗,非均质性强。孤岛化学驱油藏历程长、比重大,是存量增效主阵地孤岛油田化学驱分布图(24个项目)中一区Ng3先导区1992年中一区Ng3扩大区第一批后续水驱第二批后续水驱第三批已转后续正注项目孤岛油田储量构成图(2016)孤岛油田产量构成(2016)水驱402010%后续水驱2049050%正注聚,675416%稠油974224%水驱28.811%后续水驱50.720%正注聚81.631%稠油98.338%孤岛油田地质储量4.11亿吨,其中热采稠油动用储量0.97亿吨,化学驱动用储量2.72亿吨,累计增油1600万吨,提高采收率5.9%!其中正注聚8个、储量6754万吨,占孤岛油田的16%,产量占31%。1、积极定位存量提质增效孤岛化学驱成本较低,是调结构、提效益的主战场目前化学驱面临资源接替不足瓶颈1651078458711857372088218888019671520159014673121092880459404862-1243-3084-958-1730-1124-1701-2188-880-1047-1520-920-312-4000-20000200040006000199219931994199519961997199819992000200120022003200420052006200720082009201020112012201320142015孤岛油田“八五”以来化学驱历年投入储量情况(万吨)Ng3先导Ng3扩大中一区Ng4西区北西区复合中二南中二中先导渤19中一区Ng5-6+Ng3西北部中二中西区南西区南渤61中一区3-6渤64渤72中二北东区北中一区Ng3-6渤61渤64渤72中二中中一区Ng5-6渤19Ng3西北部西区北Ng3先导扩大中一区Ng4中二中先导中二南投注聚储量万吨转后续储量万吨东区北剩余西区北非均相扩高段塞项目5029万吨东区南渤21非均相非均相渤19-82见效初期项目1725万吨九五十五十一五十二五后续水驱项目16个:储量2.05亿吨正注项目8个:储量0.6754亿吨年均投入1870万吨年均投入469万吨八五2、深刻认识化学驱矛盾和潜力工作目标转变:化学驱主体转向高段塞、见效高峰期二类油藏项目高段塞305745%高峰期197229%见效初期,172226%孤岛油田正注化学驱项目储量构成图孤岛油田正注化学驱项目产量构成图高段塞38.339%高峰期42.543%见效初期18.118%孤岛高段塞和高峰期化学驱项目储量5029万吨,占正注储量74%,年产量占82%。工作思路转变:持续注采优化,拓宽存量项目持续发展能力孤岛油田不同批次化学驱项目日油水平变化曲线第三批储量:3487万吨41月中一区馆3先导、扩大储量:1243万吨第一批储量:6509万吨27月第二批储量:5156万吨47月第四批高段塞、高峰期项目储量:5029万吨已92月新投项目储量:1725万吨0.66.423.037.736.225.716.813.09.77.75.64.84.54.744.373.83.21.91.3214.8050100150200250051015202530354019971998199920002001200220032004200520062007200820092010201120122013201420152016累增油(万吨)年增油(万吨)时间(年)实际年增油实际累增油孤岛一类油藏中一区Ng4注聚区增油曲线提高采收率:7.5%提高采收率:4.2%↗10.4%0.5511.916.519.217.616.41514.511.810.28.46.54.32.71.81.20.80.5-10103050709011013015017002468101214161820222006200720082009201020112012201320142015201620172018201920202021202220232024累增油104t年产油104t时间年设计年增油设计累增油164.8孤岛二类油藏中二北Ng3-4注聚区增油曲线848688909294969810000.20.40.60.811.2含水%PV二类:中二北585设计二类:中二北延长一类:中一区Ng4二类中二北Ng3-4含水谷底期已108个月一类中一区Ng4含水谷底期31个月二类中二北Ng3-4设计含水谷底期26个月孤岛油田不同批次化学驱项目日油水平变化曲线第三批储量:3487万吨41月中一区馆3先导、扩大储量:1243万吨第一批储量:6509万吨27月第二批储量:5156万吨47月第四批高段塞、高峰期项目储量:5029万吨已92月新投项目储量:1725万吨0.66.423.037.736.225.716.813.09.77.75.64.84.54.744.373.83.21.91.3214.8050100150200250051015202530354019971998199920002001200220032004200520062007200820092010201120122013201420152016累增油(万吨)年增油(万吨)时间(年)实际年增油实际累增油孤岛一类油藏中一区Ng4注聚区增油曲线提高采收率:7.5%提高采收率:4.2%↗10.4%0.5511.916.519.217.616.41514.511.810.28.46.54.32.71.81.20.80.5-10103050709011013015017002468101214161820222006200720082009201020112012201320142015201620172018201920202021202220232024累增油104t年产油104t时间年设计年增油设计累增油164.8孤岛二类油藏中二北Ng3-4注聚区增油曲线848688909294969810000.20.40.60.811.2含水%PV二类:中二北585设计二类:中二北延长一类:中一区Ng4二类中二北Ng3-4含水谷底期已108个月一类中一区Ng4含水谷底期31个月二类中二北Ng3-4设计含水谷底期26个月“尖底锅”变“平底锅”孤岛化学驱含水曲线工作思路转变:持续注采优化,拓宽存量项目持续发展能力孤东采油厂孤岛采油厂•一是完善地质模型建设,深化储层、相控认识孤岛油田Ng35小层沉积相平面分布图Ng3top孤岛油田Ng3顶面构造图孤岛油田大模型建设孤岛中二北Ng3-4注聚区Ng442小层沉积相平面分布图33-42034-42032-32中二北Ng441小层沉积相平面图孤岛中二北Ng3-4注聚区Ng441小层沉积相平面分布图中二北Ng442小层沉积相平面图33-42034-42032-32理顺井网,理顺注采关系建成了孤岛大型整装油田地质模型;储层内部结构表征、韵律层的细分;高渗条带识别、剩余油分布规律;不同开发方式开发技术界限研究孤东采油厂孤岛采油厂•一是完善地质模型建设,深化储层、相控认识孤东采油厂孤岛采油厂孤岛化学驱地下流向识别划分依据渗透率(um2)孔隙度(%)连通情况原油粘度采液强度t/(d*m)累采累注状况吸水状况注采对应状况地层能量异常主流向1.537条带突破偏低10高吸水好对应好偏低正常主流向0.8—1.537—32好适中6—10高吸水好吸水较好对应好对应较好适中非主流向0.832连通性差偏高6低吸水较好吸水差对应较好对应差偏高流向分类静态因素动态因素•二是深化不同时期、动静态因素下流场认识孤东采油厂孤岛采油厂•二是深化不同时期、动静态因素下流场认识206506002065080020651000206512002065140020651600206518002065200020652200206524002065260020652800206530002065320020653400206536002065380020654000206542002065440020654600206548002065500020655200206554002065560020655800206560002065620020656400206566002065680020657000206572002065740020657600206578002065800020658200206584002065860020658800206590002065920020659400206596002065980020660000206602002066040020660600206608002066100020661200206614002066160020661800206620002066220020662400206626002066280020663000206632002066340020663600206638002066400020664200206644002066460020664800206650002066520020665400206656002066580020666000206662002066640020666600206668002066700020667200206674002065060020650800206510002065120020651400206516002065180020652000206522002065240020652600206528002065300020653200206534002065360020653800206540002065420020654400206546002065480020655000206552002065540020655600206558002065600020656200206564002065660020656800206570002065720020657400206576002065780020658000206582002065840020658600206588002065900020659200206594002065960020659800206600002066020020660400206606002066080020661000206612002066140020661600206618002066200020662200206624002066260020662800206630002066320020663400206636002066380020664000206642002066440020664600206648002066500020665200206654002066560020665800206660002066620020666400206666002066680020667000206672002066740041872004187400418760041878004188000418820041884004188600418880041890004189200418940041896004189800419000041902004190400419060041908004191000419120041914004191600419180041920004192200419240041
本文标题:化学驱优化注入提质增效的主要做法
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