Study on High Temperature Gas-Cut Resistant Weak Gel Drilling Fluid in Shunbei Oil and Gas Field
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摘要: 顺北油气田奥陶系一间房组和鹰山组的碳酸盐岩储层微裂缝发育且气层活跃,钻井液受气侵严重,主要存在油气上窜速度快,频次高,程度严重,漏涌同存等气侵特点。分析总结了顺北油气田现用防气侵方法和存在的问题,提出使用弱凝胶钻井液体系防气侵的对策。为提高该体系的抗高温性及防气侵效果,研制出高温稳定剂MG-HT、抗高温流型调节剂JHVIS、抗高温降滤失剂JHFLO和耐温封堵剂JHSEAL,并优选了其他配套处理剂,形成一套抗温效果好、堵气和承压能力强的抗高温弱凝胶防气侵钻井液体系。该体系抗温可达180 ℃,密度可达1.8 g/cm3,具有较好的流变性、降滤失性和抗污染性;此外,体系的φ6和φ3读数均大于5,低剪切速率黏度大于15 000 mPa·s,正向承压能力大于5 MPa,反向承压能力高于1 MPa,具有良好的防气侵效果。为顺北油气田碳酸盐岩裂缝性储层的安全、快速勘探和开发提供了技术支持。Abstract: The carbonate Yijianfang formation and the Yingshan formation of the Ordovician system in the Shunbei oil and gas field is developed with microfractures and active gas zones. Serious and frequent CH4 and CO2 gas cut ascended fast in the annular spaces, leading to coexistence of mud losses and well blow-out. To prevent gas cut, previous experiences obtained in the Shunbei oil and gas field were borrowed and analyzed, and a high temperature weak gel drilling fluid was developed to deal with the gas cut problem. Several additives were used to formulate this drilling fluid, such as a high temperature stabilizer MG-HT, a high temperature rheology modifier JHVIS, a high temperature filter loss reducer JHFLO and a high temperature plugging agent JHSEAL, as well as other additives selected for this drilling fluid. This drilling fluid has high temperature resistance to 180 °C, good plugging capacity to gas cut and is able to improve the pressure bearing capacity of the formations. This drilling fluid can be weighted to 1.8 g/cm3 and has good rheology, filtration property and contamination resistance. The 6-RPM and 3-RPM readings of the drilling fluid measured on a 6-speed direct-reading rheometer are both greater than 5, and the low-shear-rate viscosity of the drilling fluid is greater than 15,000 mPa·s. Formations strengthened with this drilling fluid have forward and backward pressure bearing capacities of greater than 5 MPa and 1 MPa, respectively. This weak gel drilling fluid, with good gas cut preventing capacity, has provided a technical support to the safe, fast exploration and development of the fractured carbonate reservoirs in the Shunbei oil and gas field.
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表 1 高温稳定剂加量对体系性能影响
MG-HT/
%状态 AV/
mPa·sPV/
mPa·sYP/
Paφ6/φ3 FLAPI/
mLFLHTHP/
mLLSRV/
mPa·s0 滚前 42 30 12 14/12 滚后 27 24 3 2.5/2 5.6 19.2 3200 0.5 滚前 45 32 13 14/12 滚后 34 28 6 6/4 3.2 12.6 9200 1.0 滚前 49 34 15 14/13 滚后 38 30 8 8/6 2.8 11.8 14 800 1.5 滚前 56 38 18 15/13 滚后 41 32 9 10/8 2.4 12.2 16 200 2.0 滚前 67 46 21 15/13 滚后 48 36 12 10/9 2.0 11.6 17 400 注:钻井液配方:水+65%甲酸钠+250%HCOOK+1%NaOH+0.5%Na2CO3+0.5%消泡剂Desil+1%PCD156+0.5%JHVIS+2%JHFLO+2%JHSEAL+重晶石,密度为1.80 g/cm3;实验条件:在180 ℃热滚16 h,在50 ℃测试流变性。 表 2 弱凝胶钻井液体系抗温性能评价
T/℃ 条件 AV/
mPa·sPV/
mPa·sYP/
Paφ6/φ3 FLAPI/
mLFLHTHP/
mLLSRV/
mPa·s滚前 48 32 16 14/12 120 滚后 46 30 16 13/12 1.6 60 32 000 140 滚后 52 38 14 13/11 2.0 7.4 26 500 160 滚后 58 44 14 12/10 2.6 8.2 23 300 170 滚后 52 42 10 10/8 2.6 8.8 18 800 180 滚后 50 42 8 10/8 3.0 10.6 14 800 190 滚后 40 36 4 8/6 4.6 16.2 4800 注:配方:水+60%甲酸钠+250%HCOOK+1%NaOH+0.5%Na2CO3+0.5%Desil+1%MG-HT+1%PCD156+0.5%JHVIS+2%JHFLO+2%JHSEAL+重晶石(1.80 g/cm3);条件:180 ℃ 热滚16 h后在50 ℃测试。 表 3 弱凝胶钻井液体系加重性能评价
ρ/
g·cm−3加重剂 条件 AV/
mPa·sPV/
mPa·sYP/
Paφ6/φ3 FLAPI/
mLLSRV/
mPa·s1.2 HCOONa 滚前 38 31 7 6/5 2.6 15000 1.4 HCOONa+
HCOOK滚后 44 36 8 8/6 2.6 14800 1.6 HCOONa+
HCOOK+
重晶石滚后 48 40 8 8/6 2.8 15200 1.8 HCOONa+
HCOOK+
重晶石滚后 52 43 9 10/8 2.6 15500 2.0 HCOONa+
HCOOK+
重晶石滚后 58 48 10 10/8 3.0 16800 表 4 弱凝胶钻井液体系润滑性能评价
JHSLIP/
%条件 AV/
mPa·sPV/
mPa·sYP/
Paφ6/
φ3EP FLAPI/
mLKf 0 滚后 50 40 10 10/8 0.1580 2.6 0.1326 3 滚后 68 54 14 9/7 0.0860 2.8 0.0764 表 5 弱凝胶钻井液体系抗污染性能评价
污染物 条件 AV/
mPa·sPV/
mPa·sYP/
Paφ6/
φ3FLAPI/
mLLSRV/
mPa·s0 滚后 52 42 10 10/8 2.6 15 600 2%NaCl 滚后 60 50 10 7/6 3.4 14 800 4%NaCl 滚后 68 59 9 5/4 3.2 12 400 6%NaCl 滚后 72 63 9 5/3 3.4 10 600 1%CaCl2 滚后 54 43 11 8/6 3.0 13 800 2%CaCl2 滚后 58 46 12 7/5 3.4 11 400 1%CaSO4 滚后 52 42 10 7/5 3.6 13 600 2%CaSO4 滚后 62 50 12 6/4 3.8 10 400 8%CaCl2+
4%NaCl滚后 70 61 9 5/4 3.0 11 200 5%模拟地层水 滚后 60 53 7 5/3 3.4 10 400 10%模拟地层水 滚后 48 42 6 5/3 2.8 9600 表 6 弱凝胶钻井液体系储层保护性能评价
岩心号 ρ/
g·cm−3Ko/
mDKd/
mDKd/Ko/
%酸化处理后
渗透率恢复值/%1# 1.20 10.64 8.52 80.1 90.4 2# 1.80 6.62 3.98 60.1 75.8 3# 1.80 4.93 3.08 62.5 76.6 表 7 弱凝胶钻井液体系高温高压流变性能评价
T/℃ AV/
mPa·sPV/
mPa·sYP/
PaYP/PV/
Pa/mPa·sφ6/φ3 50 52 40 12 0.30 10/8 65 51 40 11 0.28 10/8 100 47 37 10 0.27 9/7 120 43 34 9 0.26 8/6 150 38 30 8 0.27 8/5 180 30 24 6 0.25 7/5 表 8 弱凝胶钻井液体系岩心驱替封堵防气侵性能评价
缝宽/
mm正向液驱
压力/MPa完全封堵前
漏失量/mL正向气驱
压力/MPa反相气驱
压力/MPa0.02 10 0 >3 >1.0 0.05 10 0.4 >3 >1.0 0.10 10 0.8 >3 >1.2 0.20 10 0.6 >4 >2.0 0.30 10 0.2 >4 >1.8 0.40 10 0.1 >5 >2.2 0.50 10 0.4 >5 >1.8 注:钻井液配方:水+60%甲酸钠+250%HCOOK+1%NaOH+0.5%Na2CO3+0.5%消泡剂Desil+1%MG-HT+1%PCD156+0.5%JHVIS+2%JHFLO+2%JHSEAL+5%JQWY+重晶石,密度为1.80 g/cm3;钻井液在180 ℃热滚16 h。 -
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