XXX井试气压裂施工总结样本.docx

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1、鄂尔多斯盆地伊陕斜坡XXX井酸化施工总结中国石油天然气股份有限公司长庆油田分公司2019年3月1日XXX井酸化施工总结施工层位：马五4射孑L井段：3876.0-3880.0m施工队：监督单位：监督人：编 写：审 核：XXX公司压裂大队年 月日XXX井马五4层第1次酸化施工数据汇总表施工日期2018.11.15作业队S00656压裂层位马五4气层深度3875.1-3880.8 (2D)厚度(m)5.7射孔深度3876.0-3880.0厚度(m)4.0射孔枪型/弹型102-16-90-70DP44RDX38孔密(孔冰)/射孔孔数(孔)/酸化方式单上封酸化液性质稠化酸+转向酸套管尺寸139.7油管尺

2、寸88.9油管容积17.6施工步骤冲管线-试压-低压替酸-座封-稠化酸-转向酸-顶替-投球-打滑套-停泵项 目稠化酸转向酸替置液最大最小平均最大最小平均最大最小平均排量(L/min)50204980500()508049705000301029903000压力(MPa)62.747.454.358.243.051.940.828.933.4平压(MPa)19.614.416.619.111.218.510.510.210.3低替稠化酸(m3)15.6座封稠化酸(nP)： 2.0高压挤酸(nP)225.0195.017.6入地稠化酸量(n?)242.6入地转向酸量(nP)195.0入井水量(n?

3、)入地其他液量(nr3)互溶剂.入地总液量(a?)A/447.6关井时间(min)最高压力62.7Mpa停泵压力(油/套)21.4/21.3Mpa质量评定项目酸液酸液浓度数量nr?添加剂名称浓度设计用量Kg实际用量Kg方案要求稠化酸20242.6HCL209935599355转向酸20195.0HJF-941.523102310设计要求稠化酸20280.0CJ1-3 (A)0.2308308转向酸20225.0CJ1-3 (B)1.015401540设计配置稠化酸20280.0TWJ-101.015401540转向酸20225.0YFP-10.5770770施工简况钻具井深(m)施工排量(L/

4、min )酸量(n?)设计4000-4500稠化酸+转向酸：242.6+195实际45()()-5000稠化酸+转向酸：242.6+1951.施工过程中以排量200L/min伴注液氮21.0m3。2.顶替时从旋塞投40mm钢球一个。水力锚:3820. 30封隔器：3821.08节流器:3859. 39喇叭口: 3859. 53XXX井马五4层第1次酸化施工数据记录表时间工作内容排量m3/min油压Mpa套压Mpa阶段液量m3累积液量m3备注16:49冲管线0.000.100.000.00活性水16:500.0()().3()0.0()0.0016:511.250.900.00().1()16:

5、520.350.400.001.4016:531.350.800.001.9016:540.550.300.002.9016:551.550.600.0()4.0016:560.900.300.005.4016:570.850.400.006.4016:581.300.300.007.4016:591.300.600.008.7017:000.000.100.009.0017:010.000.400.109.0017:02试压0.0026.300.709.0017:030.2558.000.709.1017:040.0067.000.709.3017:050.0066.200.609.3017

6、:060.0()().100.609.3017:07低替0.400.400.609.40稠化酸17:080.403.300.609.8017:090.403.100.5010.2017:100.403.500.5()0.4017:110.403.200.0()().8()17:120.403.200.001.2017:130.001.300.001.5017:140.453.700.001.8017:150.453.100.002.3017:160.453.000.002.7017:170.453.000.003.2017:180.453.000.003.6017:190.000.800.00

7、4.0017:200.353.400.104.3017:210.353.600.004.6017:220.353.600.105.0017:230.353.500.105.3017:240.353.500.105.7017:250.353.400.106.0017:260.353.400.106.40时间工作内容排量m3/min油压Mpa套压Mpa阶段液量m3累积液量m3备注17:270.403.900.1()6.6017:280.403.100.107.0017:290.402.800.107.4017:300.402.800.107.8017:310.402.70().1()8.2017:

8、320.402.700.0()8.6017:330.402.700.009.0017:340.001.800.009.4017:350.403.800.009.7017:360.403.400.0()10.1017:37座封1.0531.800.2010.70稠化酸17:381.8040.800.1012.20互溶剂17:391.8040.402.201.1017:403.0052.1014.903.40稠化酸17:413.3()51.1019.107.6917:423.9054.4016.4012.7217:434.2050.9013.1017.7517:444.1752.3010.3022

9、.7817:454.2452.3016.6027.8217:464.4052.6016.8032.8517:474.6253.3015.4037.8817:484.8253.7014.1042.9117:495.0153.1014.1047.9417:505.0453.6017.8052.9817:515.0052.0016.9058.0117:52换酸4.9551.2016.1063.04转向酸17:534.9849.6015.4068.0717:544.9749.3015.0073.1017:554.9749.8014.6078.1417:564.9752.8019.6083.1717:5

10、74.9655.0019.1088.2017:585.0057.3018.9093.2317:594.9860.8019.0098.2718:004.9961.3018.90103.3018:015.0361.6018.70108.3318:025.0162.1018.60113.3618:03换酸5.0262.4018.5011839稠化酸18:045.0462.3018.40123.4318:054.9862.3018.40128.4618:064.9759.6018.20133.4918:075.0256.9018.10138.52时间工作内容排量m3/min油压Mpa套压Mpa阶段液量m3累积液量m3备注18:085.0353.7017.90143.5518:094.9850.4017.50148.5918:105.0047.4017.10153.6218:114.9848.1017.00158.6518:125.0148.3016.90163.6818:134.9849.5016.90168.7218:14