石油与天然气地质
石油與天然氣地質
석유여천연기지질
OIL & GAS GEOLOGY
2013年
6期
816-820
,共5页
李海成%李啸峰%高光磊%徐德奎%胡俊卿%梁福民
李海成%李嘯峰%高光磊%徐德奎%鬍俊卿%樑福民
리해성%리소봉%고광뢰%서덕규%호준경%량복민
喷嘴节流%地层渗流%流量调配%井筒管流%聚合物注入井%大庆油田
噴嘴節流%地層滲流%流量調配%井筒管流%聚閤物註入井%大慶油田
분취절류%지층삼류%류량조배%정통관류%취합물주입정%대경유전
nozzle throttle%formation seepage%flow rate allocation%wellbore conduit flow%polymer injection well%Daqing oilfield
在聚合物的注入过程中,聚合物从井口注入后在油管内流动,利用非牛顿流体力学原理建立垂向管流沿程压力损失方程。当聚合物溶液流过喷嘴时损失一部分压力与粘度。通过室内的聚合物溶液过喷嘴实验,得出了喷嘴的长径比( L/D1)及摩阻系数λ与雷诺数Re之间的关系。应用纲量分析的方法,建立了聚合物流过喷嘴后的压力损失Δp和粘度损失Δη的基本方程。结合实验数据,利用SAS软件进行回归分析,分别得到了压降及粘降关联公式。聚合物溶液流过喷嘴后进入地层,在聚合物溶液压力的作用下,聚合物溶液与岩石空隙的骨架相互挤压,聚合物的注入量也随时间逐渐降低。按照非牛顿流体在地层岩石中的渗流特点建立的单相非牛顿流体径向流的偏微分方程,结合大庆油田聚合物注入井的实际数据和前面的井筒管流、喷嘴节流产生的压力损失Δp和粘度损失Δη来束缚方程的边界条件,使用有限差分将方程离散,并应用软件求解,得出了聚合物注入压力、注入量与时间的关系,为聚合物分层配产提供了理论依据。
在聚閤物的註入過程中,聚閤物從井口註入後在油管內流動,利用非牛頓流體力學原理建立垂嚮管流沿程壓力損失方程。噹聚閤物溶液流過噴嘴時損失一部分壓力與粘度。通過室內的聚閤物溶液過噴嘴實驗,得齣瞭噴嘴的長徑比( L/D1)及摩阻繫數λ與雷諾數Re之間的關繫。應用綱量分析的方法,建立瞭聚閤物流過噴嘴後的壓力損失Δp和粘度損失Δη的基本方程。結閤實驗數據,利用SAS軟件進行迴歸分析,分彆得到瞭壓降及粘降關聯公式。聚閤物溶液流過噴嘴後進入地層,在聚閤物溶液壓力的作用下,聚閤物溶液與巖石空隙的骨架相互擠壓,聚閤物的註入量也隨時間逐漸降低。按照非牛頓流體在地層巖石中的滲流特點建立的單相非牛頓流體徑嚮流的偏微分方程,結閤大慶油田聚閤物註入井的實際數據和前麵的井筒管流、噴嘴節流產生的壓力損失Δp和粘度損失Δη來束縳方程的邊界條件,使用有限差分將方程離散,併應用軟件求解,得齣瞭聚閤物註入壓力、註入量與時間的關繫,為聚閤物分層配產提供瞭理論依據。
재취합물적주입과정중,취합물종정구주입후재유관내류동,이용비우돈류체역학원리건립수향관류연정압력손실방정。당취합물용액류과분취시손실일부분압력여점도。통과실내적취합물용액과분취실험,득출료분취적장경비( L/D1)급마조계수λ여뢰낙수Re지간적관계。응용강량분석적방법,건립료취합물류과분취후적압력손실Δp화점도손실Δη적기본방정。결합실험수거,이용SAS연건진행회귀분석,분별득도료압강급점강관련공식。취합물용액류과분취후진입지층,재취합물용액압력적작용하,취합물용액여암석공극적골가상호제압,취합물적주입량야수시간축점강저。안조비우돈류체재지층암석중적삼류특점건립적단상비우돈류체경향류적편미분방정,결합대경유전취합물주입정적실제수거화전면적정통관류、분취절유산생적압력손실Δp화점도손실Δη래속박방정적변계조건,사용유한차분장방정리산,병응용연건구해,득출료취합물주입압력、주입량여시간적관계,위취합물분층배산제공료이론의거。
In the process of polymer flooding , polymer solution flows first through tubes in wellbore after injected from wellhead .A vertical conduit flow frictional pressure loss equation is set up according to the theory of non -Newtonian fluid mechanics.Usually,a part of pressure and viscosity will be lost when the polymer solution flows through a nozzle .The re-lationships of nozzle length to diameter ratio ( L/D1 ) with friction coefficient (λ) and Reynolds number ( Re) can be estab-lished through experiment modeling the process of polymer solution flowing through nozzle .The basic equations of pres-sure lossΔp and viscosity loss Δηare developed by using dimension analysis method .In combination with the experimen-tal data ,an incidence formula of pressure drawdown and dynamic viscosity loss can be built through regression analysis with SAS software .After polymer solution enters strata ,it will squeeze the skeleton of rock under pressure of polymer so-lution and the injection rate will also decrease with time .Partial differential equations of single phase radial flow of non-Newtonian fluid is established according to the seepage characteristics of non-Newtonian flow .The equations are discrete by using the finite difference and solved by software with the boundary conditions of the equations constrained by the real data,pressure drawdown and dynamic viscosity loss caused by conduit flow and throttled flow .The relationships between injection pressure ,injection rate and time are established ,providing a theoretical basis for separate-layer polymer injection rate allocation.