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METHOD FOR PRODUCTION OF HIGH-TECHNOLOGY OIL AND TECHNOLOGICAL COMPLEX FOR ITS IMPLEMENTATION

机译:实现高技术油和技术复合物的方法

摘要

FIELD: mining.;SUBSTANCE: group of inventions relates to production of natural bitumen, heavy and high-viscosity oil. Method of oil production includes formation of near-borehole zone with high permeability due to injection into the near-borehole zone of working input agent (WIA) in form of water with temperature higher than 593 °C at pressure from 23 to 50 MPa, generating WIA high-tech oil in the borehole zone with subsequent extraction thereof, then successively performing three cycles of thermochemical impact, each of which includes three successive steps. At first stage of first cycle, injection is performed WIA in form of water with temperature higher than 593 °C and pressure from 23 to 50 MPa, saturated with Fenton's reagent. At the second stage of the first cycle, injection WIA in form of water with temperature from 380 to 593 °C at pressure from 23 to 50 MPa with subsequent extraction at the third stage of this oil cycle. At the first stage of the second cycle sequential injection WIA, consisting of water with temperature from 380 to 593 °C at pressure from 23 to 50 MPa, saturated with Fenton reagent, which consists of hydrogen peroxide and catalyst in form of iron ions II or III, and WIA in form of water with temperature higher than 593 °C at pressure from 23 to 50 MPa, saturated with hydrogen peroxide and hydrogen peroxide inhibitor, or WIA in form of water with temperature from 380 to 593 °C at pressure from 23 to 50 MPa, saturated with hydrogen peroxide and hydrogen peroxide inhibitor. At the second stage of the second cycle, injection WIA, consisting of water with temperature higher than 593 °C at pressure from 23 to 50 MPa, or WIA, consisting of water with temperature from 380 to 593 °C at pressure from 23 to 50 MPa, with subsequent extraction at the third stage of this oil cycle. At the first stage of the third cycle sequential injection WIA in form of water with temperature higher than 593 °C at pressure from 23 to 50 MPa, saturated with hydrogen peroxide, or WIA in form of water with temperature from 380 to 593 °C at pressure from 23 to 50 MPa, saturated with hydrogen peroxide. At the second stage of the third cycle, injection WIA, consisting of water with temperature higher than 593 °C at pressure from 23 to 50 MPa, or WIA in form of water with temperature from 380 to 593 °C at pressure from 23 to 50 MPa with subsequent extraction at the third stage of this oil cycle. Technological complex for oil production includes water treatment plant, generator for water production with pressure higher than 23 MPa and temperature higher than 593 °C, a column of heat-insulated tubing string (TS), container for storage and dispensing of treated water, 30–40 % hydrogen peroxide, water saturated with a catalyst in form of iron ions II, water saturated with a hydrogen inhibitor, WIA, working input agents. Compensator of thermobaric changes in length of tubing string is built in tubing string. Outer surface of compensator has possibility of tight contact with inner surface of casing pipe.;EFFECT: higher oil recovery of formations, formation of high-permeable in-situ retort, constant recovery of permeability in the borehole zone.;2 cl, 4 dwg, 1 tbl
机译:技术领域:发明组涉及天然沥青,重质和高粘度油的生产。采油的方法包括由于在23至50 MPa的压力下以高于593°C的水的形式注入工作输入剂(WIA)的近井区而形成高渗透率的近井区,产生钻孔区域中的WIA高科技油及其随后的提取,然后依次执行三个热化学冲击循环,每个循环包括三个连续步骤。在第一个循环的第一阶段,以水的形式进行WIA注射,温度高于593°C,压力为23至50 MPa,并用Fenton试剂饱和。在第一个循环的第二阶段,以23至50 MPa的压力在380至593°C的温度下注入水形式的WIA,随后在该油循环的第三阶段进行萃取。在第二个周期的顺序注射WIA的第一阶段,由温度为380至593°C,压力为23至50 MPa的水组成,并用Fenton试剂饱和,该试剂由过氧化氢和铁离子II或II形式的催化剂组成III和WIA在23至50 MPa的压力下温度高于593°C的水形式,用过氧化氢和过氧化氢抑制剂饱和的WIA或WIA在23至压力下的温度在380至593°C的水形式的WIA至50 MPa,用过氧化氢和过氧化氢抑制剂饱和。在第二个循环的第二阶段,注入WIA,由压力在23至50 MPa时温度高于593°C的水组成,或WIA,由温度在23至50压力下从380至593°C的水组成MPa,随后在该油循环的第三阶段提取。在第三周期的第一阶段,以23至50 MPa的压力,温度高于593°C的水的形式依次注入WIA,并用过氧化氢饱和;或者以380至593°C的温度以水的形式的WIA以水的形式注入WIA压力为23至50 MPa,并用过氧化氢饱和。在第三个循环的第二阶段,注入WIA,由温度在23至50 MPa的压力下高于593°C的水组成,或在23至50的压力下以温度在380至593°C的水形式的WIA组成MPa,随后在该油循环的第三阶段提取。石油生产的技术设施包括水处理厂,压力高于23 MPa,温度高于593°C的水生产发电机,一列隔热油管(TS),用于存储和分配经处理水的容器30 –40%的过氧化氢,用铁离子II形式的催化剂饱和的水,用氢抑制剂,WIA饱和的水,有效的输入试剂。油管柱中的热压长度变化补偿器内置在油管柱中。补偿器的外表面可能与套管的内表面紧密接触。效果:地层的采油率更高,形成高渗透性的原形馏分,在井眼区域的渗透率不断恢复。2 cl,4 dwg ,1汤匙

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