CN108716391A - A method of it recovers the oil and is regulated and controled with endogenous microbes group - Google Patents

A method of it recovers the oil and is regulated and controled with endogenous microbes group Download PDF

Info

Publication number
CN108716391A
CN108716391A CN201810481543.8A CN201810481543A CN108716391A CN 108716391 A CN108716391 A CN 108716391A CN 201810481543 A CN201810481543 A CN 201810481543A CN 108716391 A CN108716391 A CN 108716391A
Authority
CN
China
Prior art keywords
activator
aerobic
reservoir
experiment
oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201810481543.8A
Other languages
Chinese (zh)
Other versions
CN108716391B (en
Inventor
束青林
刘涛
曹嫣镔
宋永亭
冯云
胡婧
李彩风
高光军
郭辽原
孙刚正
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Chemical Corp
Sinopec Research Institute of Petroleum Engineering Shengli Co
Original Assignee
China Petroleum and Chemical Corp
Sinopec Research Institute of Petroleum Engineering Shengli Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Petroleum and Chemical Corp, Sinopec Research Institute of Petroleum Engineering Shengli Co filed Critical China Petroleum and Chemical Corp
Priority to CN201810481543.8A priority Critical patent/CN108716391B/en
Publication of CN108716391A publication Critical patent/CN108716391A/en
Application granted granted Critical
Publication of CN108716391B publication Critical patent/CN108716391B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B49/00Testing the nature of borehole walls; Formation testing; Methods or apparatus for obtaining samples of soil or well fluids, specially adapted to earth drilling or wells

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • Physics & Mathematics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Measuring Or Testing Involving Enzymes Or Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

The invention belongs to technical field of tertiary oil recovery, and in particular to a kind of regulation and control method recovered the oil with endogenous microbes group.The present invention carries out the screening of experiment oil reservoir first, simulation core parameter is determined according to the condition of experiment oil reservoir, and then carry out the physical simulation experiment of experiment oil reservoir, microbiologic population's regularity of distribution is determined according to experiment reservoir physical simulation experimental result, to clear different type microorganism activator injection amount and live injection technology, field test is finally carried out.The present invention can effectively different types of microorganism in activation experiment oil reservoir, simultaneously effective reduce the cost of investment of microorganism activator, to realize the recovery ratio for increasing substantially experiment oil reservoir, field test results are apparent, input-output ratio 1:12 or more, it improves recovery ratio and is more than 20%.

Description

A method of it recovers the oil and is regulated and controled with endogenous microbes group
Technical field
The invention belongs to technical field of tertiary oil recovery, and in particular to a kind of side regulated and controled with endogenous microbes group of recovering the oil Method.
Background technology
The endogenous microbes displacement of reservoir oil refers to using the microbiologic population's system formed during oil reservoir long-term injecting water, by note The microbiologic population in activator activation oil reservoir, the surface reactive material generated using microorganism itself and metabolism are injected in well It has an effect with biogas and the crude oil in oil reservoir, improves crude output and recovery ratio, be an environmental protection, inexpensive exploitation skill Art.
Endogenous microbes are sequentially distributed aerobic microbiological, facultative aerobic microbiological in oil reservoir from water injection well to producing well And anaerobe, different types of microorganism run through entire oil reservoir, different type microorganism and its metabolite jointly with oil Crude oil effect in Tibetan, to generate oil displacement efficiency.Although but being noted from water injection well in endogenous microbes oil displacement process at present Enter different types of microorganism activator activation aerobic microbiological, facultative aerobic microbiological and anaerobe, but it is different The activator of type is to inject oil reservoir from water injection well, and there are Adsorption And Retention effects for one side activator itself, on the other hand not There is overlapping in same type activator, influence effective activation of microorganism.Therefore, it is necessary to the micro- lifes of different type in clear oil reservoir The regularity of distribution of object, and then realize the accurate injection of different type microorganism activator, realize effectively activation.
By literature search, notification number " CN104481476A ", a kind of patent name " microbial oil displacement raising oil recovery factor Method ", disclosing a kind of method that microbial oil displacement improves oil recovery factor will be micro- by detecting endogenous microbes type The biological displacement of reservoir oil has been divided into stages aerobic, facultative, that the anaerobe displacement of reservoir oil is different.But the disadvantages of this method is:(1) in oil reservoir Different type microorganism include aerobic, facultative aerobic and anaerobe be it is simultaneous from water injection well to producing well, can not The microorganism activation displacement of reservoir oil of a certain type can be only existed;(2) the different microorganisms displacement of reservoir oil stage is injected by water injection well in oil reservoir, And it is not injected into the difference of speed and injection mode, activator is mainly consumed utilization in oil reservoir middle front part, is unfavorable for oil reservoir The activation of medium and deep microorganism;(3) bacterium solution that injection different type microorganism is also needed in the above method, needs to micro- life Object is screened, is cultivated, is fermented, and implementation process complexity is cumbersome, is unfavorable for field conduct, but also asking there are oil reservoir conformability Topic.
Invention content
The purpose of the present invention is provide a kind of oil recovery endogenous microbes group tune in view of the above shortcomings of the prior art The method of control.The present invention carries out the screening of experiment oil reservoir first, determines simulation core parameter according to the condition of experiment oil reservoir, in turn The physical simulation experiment for carrying out experiment oil reservoir determines microbiologic population's distribution rule according to experiment reservoir physical simulation experimental result Rule finally carries out field test to clear different type microorganism activator injection amount and live injection technology.The present invention Can effectively different types of microorganism in activation experiment oil reservoir, simultaneously effective reduce the investment of microorganism activator at This, to realize that the recovery ratio for increasing substantially experiment oil reservoir, field test results are apparent.
The invention discloses a kind of methods that oil recovery is regulated and controled with endogenous microbes group, which is characterized in that specifically include with Lower step, but it is not limited to following steps:
(1) screening of oil reservoir is tested
It is necessary to meet following condition for the screening of experiment oil reservoir:90 DEG C of reservoir temperature <, reservoir pressure < 20MPa, permeability > 100 × 10-3μm2, reservoir formation water salinity < 200000mg/L and Reservoir Crude Oil viscosity < 50000mPas.
(2) determination of experimental simulation core parameters
Experimental simulation core parameters include:Rock core length, diameter and sample point;
Experimental simulation rock core length:It is 100- that the distance between oil reservoir oil-water well, which is tested, with experimental simulation rock core length ratio 200:1;
Experimental simulation core diameter:It is 50-80 to test reservoir thickness and experimental simulation core diameter ratio:1;
Experimental simulation boring sample point:Sample point quantity is that a sample point is arranged at interval of 0.1m-0.2m, and sample point is equal It is even to be distributed on experimental simulation rock core.
(3) physical simulation experiment of oil reservoir is tested
Using above-mentioned experimental simulation rock core carry out experiment oil reservoir physical simulation experiment, experiment the specific steps are:
Load experimental simulation rock core identical with experiment Reservoir Permeability;Simulation core vacuumizes, saturation testing oil reservoir Water flooding;The dehydration degassed crude of saturation testing oil reservoir;Experimental simulation rock core is placed under experiment reservoir temperature and pressure condition 10d, then carries out a water drive, and a water drive is extremely aqueous consistent with experiment oil reservoir current composite;Experimental simulation boring sample point It is sampled, each sample point sampling amount is 10-20mL;Aerobic, the facultative aerobic and anaerobe content of test sample.
(4) in experimental simulation rock core microbiologic population's regularity of distribution determination
According to above-mentioned test result, aerobic, facultative aerobic and anaerobe distribution rule in experimental simulation rock core are analyzed Rule determines aerobic and facultative aerobic, the facultative aerobic separation with anaerobe.
(5) determination of microbiologic population's regularity of distribution in oil reservoir is tested
Aerobic and facultative aerobic, the facultative aerobic separation with anaerobe, the Yi Jishi determined according to above-mentioned steps The ratio for testing the distance between oil reservoir oil-water well and experimental simulation rock core length, determine respectively experiment oil reservoir in it is aerobic with it is facultative Aerobic separation and water injection well distance L1, facultative aerobic separation and water injection well distance L with anaerobe2
(6) determination of activator injection amount
Activator includes aerobic microbiological activator, facultative aerobic microbiological activator and anaerobe activator.
(7) determination of activator scene injection technology
Activator scene injection technology be in the experiment oil reservoir determined according to above-mentioned steps it is aerobic with it is facultative aerobic and simultaneous Facultative aerobic and anaerobe activator note is respectively set at aerobic position corresponding with the separation of anaerobe in property Entrance, facultative aerobic and anaerobe activator are injected from above-mentioned inlet respectively, and aerobic microbiological activator is oily from experiment It is injected in the water injection well of Tibetan.
(8) field test and effect assessment
Field test is carried out according to above-mentioned determining activator injection amount and activator scene injection technology, after the test Statistics and the analysis for carrying out field test results, calculate the raising recovery ratio value and input-output ratio of experiment oil reservoir.
The aerobic microbiological includes bacillus subtilis, pseudomonas aeruginosa and acinetobacter calcoaceticus.
The facultative aerobic microbiological includes ground bacillus, beam hanger bacterium and achromobacter.
The anaerobe includes methanogen, nitrate reduction bacterium and anaerobism dialister bacterium.
The aerobic microbiological activator is starch 1.5-2.0wt%, peptone 0.9-1.2wt%, dipotassium hydrogen phosphate 0.3-0.6wt%, hydrogen peroxide 1.0-1.5wt%.
The facultative aerobic microbiological activator be glucose 1.8-2.2wt%, Dried Corn Steep Liquor Powder 1.0-1.4wt%, Disodium hydrogen phosphate 0.4-0.8wt%.
The anaerobe activator is starch 1.5-2.0wt%, Dried Corn Steep Liquor Powder 0.5-0.8wt%, phosphoric acid hydrogen Diamino 0.3-0.6wt%.
The determination of the aerobic microbiological activator injection amount is as follows:
V1=R2L1Фβ1
In formula:V1- aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness, m;
L1- aerobic at a distance from facultative aerobic separation and water injection well, m;
The porosity of Ф-experiment oil reservoir, dimensionless;
β1- use level coefficient, dimensionless, value range are 0.5~0.6.
The determination of the facultative aerobic microbiological activator injection amount is as follows:
V2=R2(L2-L1)Фβ2
In formula:V2- facultative aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness, m;
L1- aerobic at a distance from facultative aerobic separation and water injection well, m;
L2At a distance from-facultative aerobic separation and water injection well with anaerobe, m;
Ф-reservoir pore degree, dimensionless;
β2- use level coefficient, dimensionless, value range are 0.8~1.0.
The determination of the anaerobe activator injection amount is as follows:
V3=R2(L-L2)Фβ3
In formula:V3- anaerobe activator injection amount, m3
R-experiment reservoir thickness, m;
L-experiment oil reservoir injection well is at a distance from oil well, m;
L2At a distance from-facultative aerobic separation and water injection well with anaerobe, m;
Ф-reservoir pore degree, dimensionless;
β3- use level coefficient, dimensionless, value range are 0.6~0.8.
The present invention has the following advantages that compared with prior art and advantageous effect:
(1) specify that different location is aerobic, facultative aerobic in experiment oil reservoir by simulated experiment using experimental simulation rock core And the distributed areas of anaerobe, the design for activator injection amount provide foundation;
(2) activator that different type microorganism is injected from experiment oil reservoir different location, improves activator activating microorganisms Specific aim and validity, to improve the oil displacement efficiency of microorganism, input-output ratio 1:12 or more, it is big to improve recovery ratio In 20%;
(3) activator system is oriented activation according to distributed areas of the microorganism in testing oil reservoir, effectively prevents The absorption and delay of activator component, save activator cost;
(4) specific aim and operability of the method field conduct are strong, the production low with cost of winning compared with conventional method Go out the advantages that liquid is without subsequent processing, safety and environmental protection.
Specific implementation mode
With reference to specific embodiment, the present invention is described in further detail:
Embodiment 1:
Test block A overviews in Shengli Oil Field oil recovery factory:65 DEG C, reservoir pressure 11MPa of reservoir temperature, core intersection 6.5m, permeability 800 × 10-3μm2, formation water salinity 8500mg/L, porosity 26%, viscosity of crude 1200mPas is comprehensive Aqueous 93.5% is closed, recovery percent of reserves 24.0%, average well spacing is 240m.Carry out micro- life in the oil reservoir using the method for the present invention The object displacement of reservoir oil, is as follows:
(1) screening of oil reservoir is tested
Reservoir temperature is 65 DEG C, reservoir pressure 11MPa, Reservoir Permeability are 800 × 10-3μm2, formation water salinity be 8500mg/L, viscosity of crude 1200mPas.Meet the screening criteria of the experiment oil reservoir of the present invention, therefore this hair can be implemented It is bright.
(2) determination of experimental simulation core parameters
Experimental simulation rock core length:The distance between oil-water well is 240m, the distance between experiment oil reservoir oil-water well and reality It is 100 to test simulation core length ratio:1, the length for calculating rock core is 2.4m.
Experimental simulation core diameter:Reservoir thickness is 6.5m, tests reservoir thickness and experimental simulation core diameter ratio 50: 1, it is 0.13m to calculate core diameter.
Experimental simulation boring sample point:Rock core length is 2.4m, and 0.2m is divided between sample point, and design sample points are 12 It is a.
(3) physical simulation experiment of oil reservoir is tested
Using above-mentioned experimental simulation rock core carry out experiment oil reservoir physical simulation experiment, experiment the specific steps are:1. according to Oil reservoir A conditions load rock core, and rock core basic demand is permeability 800 × 10-3μm2, porosity 26%, saturated pool water flooding, Saturated pool is dehydrated degassed crude, and rock core is simulated oil reservoir aging at temperature and placed 10 days;2. water drive of rock core, a water drive extraction Degree 24%, Produced Liquid aqueous 93.5%;3. carry out microbiological analysis is sampled to 12 sample points of rock core after a water drive, Specific data are as shown in table 1 below:
The dense variation of different type microbial bacteria in 1 boring sample point production fluid of table
(4) in experimental simulation rock core microbiologic population's regularity of distribution determination
According to above-mentioned test result, rock core displacement test analysis result shows that aerobic microbiological is mainly distributed on the 1 of rock core Region between number-No. 3 sample points, facultative aerobic microbiological are mainly distributed on the region between No. 4-No. 7 sample points of rock core, detest Oxygen animalcule is mainly distributed on the region between No. 8-No. 12 sample points of rock core.So being advised according to the distribution of different zones microorganism Rule determines aerobic and facultative aerobic microbiological separation apart from the position of core entry 0.6m, the facultative aerobic and micro- life of anaerobism The separation of object is apart from the position of core entry 1.4m.
(5) determination of microbiologic population's regularity of distribution in oil reservoir is tested
Aerobic and facultative aerobic, the facultative aerobic separation with anaerobe, the Yi Jishi determined according to above-mentioned steps Test the ratio 100 of the distance between oil reservoir oil-water well and experimental simulation rock core length:1, determine experiment oil reservoir in it is aerobic with it is simultaneous Property aerobic separation and water injection well distance L1For 60m, facultative aerobic separation and water injection well with anaerobe away from From L2For 140m.
(6) determination of activator injection amount
Activator includes aerobic microbiological activator, facultative aerobic microbiological activator and anaerobe activator.Its Middle aerobic microbiological activator is:Starch 1.5wt%, peptone 1wt%, dipotassium hydrogen phosphate 0.3wt%, hydrogen peroxide 1.5wt%, The determination of aerobic microbiological activator injection amount is as follows:
V1=3.14R2L1Фβ1=1035m3
In formula:V1- aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness 6.5m;
L1- injection well to the aerobic distance between facultative aerobic microbiological separation be 60m;
Ф-reservoir pore degree 0.26;
β1- use level coefficient, dimensionless, value 0.5.
Facultative aerobic microbiological activator is glucose 2.2wt%, Dried Corn Steep Liquor Powder 1.2wt%, disodium hydrogen phosphate The determination of 0.6wt%, facultative aerobic microbiological activator injection amount are as follows:
V2=3.14R2(L2-L1)Фβ2=2483m3
In formula:V2- facultative aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness 6.5m;
L1- aerobic with facultative aerobic separation and water injection well distance 60m;
L2- facultative aerobic separation and water injection well distance 140m with anaerobe;
Ф-reservoir pore degree 0.26;
β2- use level coefficient, dimensionless, value 0.9.
Anaerobe activator is starch 1.6wt%, Dried Corn Steep Liquor Powder 0.7wt%, dihydrogen phosphate 0.5wt%, is detested The determination of oxygen animalcule activator injection amount is as follows:
V3=3.14R2(L-L2)Фβ3=2424.5m3
In formula:V3- anaerobe activator injection amount, m3
R-experiment reservoir thickness 6.5m;
L-experiment oil reservoir injection well and oil well distance 240m;
L2- facultative aerobic separation and water injection well distance 140m with anaerobe;
Ф-reservoir pore degree 0.26;
β3- use level coefficient, dimensionless, value 0.7.
(7) determination of activator injection technique
Activator scene injection technology be in the experiment oil reservoir determined according to above-mentioned steps it is aerobic with it is facultative aerobic and simultaneous Facultative aerobic and anaerobe activator note is respectively set at aerobic position corresponding with the separation of anaerobe in property Entrance, wherein aerobic microbiological activator are injected from the water injection well of experiment oil reservoir, and facultative aerobic microbiological activator is from distance The inlet of water injection well 60m injects, and anaerobe activator is injected from the inlet apart from water injection well 140m.
(8) field test and effect assessment
Block comprehensive water cut drops to 76.5% by 93.5% after field test, aqueous to reduce by 17 percentage points, increasing Produce crude oil 2.5 × 104T improves recovery ratio 21.8%, input-output ratio 1:10.5, field test results are good.
Embodiment 2
Test block B overviews in Shengli Oil Field oil recovery factory:80 DEG C, reservoir pressure 15MPa, core intersection 4m of reservoir temperature, Permeability 1200 × 10-3μm2, formation water salinity 10500mg/L, porosity 28%, viscosity of crude 850mPas, synthesis contain Water 94.8%, recovery percent of reserves 30%, average well spacing are 200m.Carry out endogenous microbes in the oil reservoir using the method for the present invention The displacement of reservoir oil is as follows:
(1) screening of oil reservoir is tested
Reservoir temperature is 80 DEG C, reservoir pressure 15MPa, Reservoir Permeability are 1200 × 10-3μm2, formation water salinity For 10500mg/L, viscosity of crude 850mPas.Meet the screening criteria of the experiment oil reservoir of the present invention, therefore this can be implemented Invention.
(2) determination of experimental simulation core parameters
Experimental simulation rock core length:The distance between oil-water well is 200m, the distance between experiment oil reservoir oil-water well and reality Test simulation core length ratio 200:1, it is 1m to calculate rock core length.
Experimental simulation core diameter:Reservoir thickness is 4m, tests reservoir thickness and experimental simulation core diameter ratio 50:1, It is 0.08m to calculate core diameter.
Experimental simulation boring sample point:Rock core length is 2m, and 0.1m is divided between sample point, and it is 10 to calculate number of sampling It is a.
(3) physical simulation experiment of oil reservoir is tested
Using above-mentioned experimental simulation rock core carry out experiment oil reservoir physical simulation experiment, experiment the specific steps are:1. according to Oil reservoir B conditions load rock core, and rock core basic demand is permeability 1200 × 10-3μm2, porosity 28%, saturated pool water flooding, Saturated pool is dehydrated degassed crude, and rock core is simulated reservoir temperature and placed 10 days;2. water drive of rock core, a water drive recovery percent of reserves 30%, Produced Liquid aqueous 94.8%;3. being sampled carry out microbiological analysis to 10 sample points of rock core after a water drive, specifically Data are as shown in table 2 below:
The dense variation of different type microbial bacteria in 2 boring sample point production fluid of table
(4) in experimental simulation rock core microbiologic population's regularity of distribution determination
According to above-mentioned test result, rock core displacement test analysis result shows that aerobic microbiological is mainly distributed on the 1 of rock core Region between number-No. 3 sample points, facultative aerobic microbiological are mainly distributed on the region between No. 4-No. 6 sample points of rock core, detest Oxygen animalcule is mainly distributed on the region between No. 7-No. 10 sample points of rock core.So being advised according to the distribution of different zones microorganism Rule determines aerobic and facultative aerobic microbiological separation apart from the position of core entry 0.3m, the facultative aerobic and micro- life of anaerobism The separation of object is apart from the position of core entry 0.6m.
(5) determination of microbiologic population's regularity of distribution in oil reservoir is tested
Aerobic and facultative aerobic, the facultative aerobic separation with anaerobe, the Yi Jishi determined according to above-mentioned steps The ratio for testing the distance between oil reservoir oil-water well and experimental simulation rock core length, determine experiment oil reservoir in it is aerobic with it is facultative aerobic Separation and water injection well distance L1For 60m, facultative aerobic separation and water injection well distance L with anaerobe2For 120m。
(6) determination of activator injection amount
Activator includes aerobic microbiological activator, facultative aerobic microbiological activator and anaerobe activator.Its Middle aerobic microbiological activator is:Starch 1.7wt%, peptone 1.1wt%, dipotassium hydrogen phosphate 0.4wt%, hydrogen peroxide The determination of 1.3wt%, aerobic microbiological activator injection amount are as follows:
V1=3.14R2L1Фβ1=506m3
In formula:V1- aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness 4m;
L1- injection well to the aerobic distance between facultative aerobic microbiological separation be 60m;
Ф-reservoir pore degree 0.28;
β1- use level coefficient, dimensionless, value 0.6.
Facultative aerobic microbiological activator is glucose 1.9wt%, Dried Corn Steep Liquor Powder 1.3wt%, disodium hydrogen phosphate The determination of 0.5wt%, facultative aerobic microbiological activator injection amount are as follows:
V2=3.14R2(L2-L1)Фβ2=759m3
In formula:V2- facultative aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness 4m;
L1- aerobic with facultative aerobic separation and water injection well distance 60m;
L2- facultative aerobic separation and water injection well distance 120m with anaerobe;
Ф-reservoir pore degree 0.28;
β2- use level coefficient, dimensionless, value 0.9.
Anaerobe activator is starch 1.8wt%, Dried Corn Steep Liquor Powder 0.8wt%, dihydrogen phosphate 0.6wt%, is detested The determination of oxygen animalcule activator injection amount is as follows:
V3=3.14R2(L-L2)Фβ3=900m3
In formula:V3- anaerobe activator injection amount, m3
R-experiment reservoir thickness 4m;
L-experiment oil reservoir injection well and oil well distance 200m;
L2- facultative aerobic separation and water injection well distance 120m with anaerobe;
Ф-reservoir pore degree 0.28;
β3- use level coefficient, dimensionless, value 0.8.
(7) determination of activator injection technique
Activator scene injection technology be in the experiment oil reservoir determined according to above-mentioned steps it is aerobic with it is facultative aerobic and simultaneous Facultative aerobic and anaerobe activator note is respectively set at aerobic position corresponding with the separation of anaerobe in property Entrance, wherein aerobic microbiological activator are injected from the water injection well of experiment oil reservoir, and facultative aerobic microbiological activator is from distance The inlet of water injection well 60m injects, and anaerobe activator is injected from the inlet apart from water injection well 120m.
(8) statistics of field test results and analysis
Block comprehensive water cut drops to 84.5% by 94.8% after field test, aqueous to reduce by 10.3 percentage points, Incremental oil production 3.2 × 104T improves recovery ratio 22.5%, input-output ratio 1:12.0, field test results are good.
Embodiment 3:
Test block C overviews in Shengli Oil Field oil recovery factory:75 DEG C, reservoir pressure 12.5MPa of reservoir temperature, core intersection 10m, permeability 1050 × 10-3μm2, formation water salinity 9400mg/L, porosity 32%, viscosity of crude 690mPas, synthesis Aqueous 89%, recovery percent of reserves 24%, average well spacing is 300m.Carry out endogenous microbes in the oil reservoir using the method for the present invention Oil displacement test is as follows:
(1) screening of oil reservoir is tested
Reservoir temperature is 75 DEG C, reservoir pressure 12.5MPa, Reservoir Permeability are 1050 × 10-3μm2, water flooding mineralising Degree is 9400mg/L, viscosity of crude 690mPas.Meet the screening criteria of the experiment oil reservoir of the present invention, therefore can implement The present invention.
(2) determination of experimental simulation core parameters
Experimental simulation rock core length:The distance between oil-water well is 300m, the distance between experiment oil reservoir oil-water well and reality Test simulation core length ratio 100:1, calculate rock core length 3m.
Experimental simulation core diameter:Reservoir thickness is 10m, tests reservoir thickness and experimental simulation core diameter ratio 80: 1, it is 0.125m to calculate core diameter.
Experimental simulation boring sample point:Rock core length is 3m, and 0.2m is divided between sample point, and it is 15 to calculate number of sampling It is a.
(3) physical simulation experiment of oil reservoir is tested
Using above-mentioned experimental simulation rock core carry out experiment oil reservoir physical simulation experiment, experiment the specific steps are:1. according to Oil reservoir C conditions load rock core, and rock core basic demand is permeability 1050 × 10-3μm2, porosity 32%, saturated pool water flooding, Saturated pool is dehydrated degassed crude, and rock core is simulated reservoir temperature and placed 10 days;2. water drive of rock core, a water drive recovery percent of reserves 24%, Produced Liquid aqueous 89%;3. being sampled carry out microbiological analysis to 15 sample points of rock core after a water drive, specific number According to as shown in table 3 below:
The dense variation of different type microbial bacteria in 3 boring sample point production fluid of table
(4) in experimental simulation rock core microbiologic population's regularity of distribution determination
According to above-mentioned test result, rock core displacement test analysis result shows that aerobic microbiological is mainly distributed on the 1 of rock core Region between number-No. 5 sample points, facultative aerobic microbiological are mainly distributed on the region between No. 6-No. 11 sample points of rock core, Anaerobe is mainly distributed on the region between No. 12-No. 15 sample points of rock core.So according to point of different zones microorganism Cloth rule determines the aerobic separation with facultative aerobic microbiological apart from the position of core entry 1m, facultative aerobic micro- with anaerobism The separation of biology is apart from the position of core entry 2.2m.
(5) determination of microbiologic population's regularity of distribution in oil reservoir is tested
Aerobic and facultative aerobic, the facultative aerobic separation with anaerobe, the Yi Jishi determined according to above-mentioned steps The ratio for testing the distance between oil reservoir oil-water well and experimental simulation rock core length, determine experiment oil reservoir in it is aerobic with it is facultative aerobic Separation and water injection well distance L1For 100m, facultative aerobic separation and water injection well distance L with anaerobe2For 220m。
(6) determination of activator injection amount
Activator includes aerobic microbiological activator, facultative aerobic microbiological activator and anaerobe activator.Its Middle aerobic microbiological activator is:Starch 1.8wt%, peptone 0.9wt%, dipotassium hydrogen phosphate 0.5wt%, hydrogen peroxide The determination of 1.5wt%, aerobic microbiological activator injection amount are as follows:
V1=3.14R2L1Фβ1=5024m3
In formula:V1- aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness 10m;
L1- injection well to the aerobic distance between facultative aerobic microbiological separation be 100m;
Ф-reservoir pore degree 0.32;
β1- use level coefficient, dimensionless, value 0.5.
Facultative aerobic microbiological activator is glucose 2wt%, Dried Corn Steep Liquor Powder 1.3wt%, disodium hydrogen phosphate The determination of 0.5wt%, facultative aerobic microbiological activator injection amount are as follows:
V2=3.14R2(L2-L1)Фβ2=9646m3
In formula:V2- facultative aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness 10m;
L1- aerobic with facultative aerobic separation and water injection well distance 100m;
L2- facultative aerobic separation and water injection well distance 220m with anaerobe;
Ф-reservoir pore degree 0.32;
β2- use level coefficient, dimensionless, value 0.8.
Anaerobe activator is starch 1.5wt%, Dried Corn Steep Liquor Powder 0.6wt%, dihydrogen phosphate 0.4wt%, is detested The determination of oxygen animalcule activator injection amount is as follows:
V3=3.14R2(L-L2)Фβ3=4823m3
In formula:V3- anaerobe activator injection amount, m3
R-experiment reservoir thickness 10m;
L-experiment oil reservoir injection well and oil well distance 300m;
L2- facultative aerobic separation and water injection well distance 220m with anaerobe;
Ф-reservoir pore degree 0.32;
β3- use level coefficient, dimensionless, value 0.6.
(7) determination of activator injection technique
Activator scene injection technology be in the experiment oil reservoir determined according to above-mentioned steps it is aerobic with it is facultative aerobic and simultaneous Facultative aerobic and anaerobe activator note is respectively set at aerobic position corresponding with the separation of anaerobe in property Entrance, wherein aerobic microbiological activator are injected from the water injection well of experiment oil reservoir, and facultative aerobic microbiological activator is from distance The inlet of water injection well 100m injects, and anaerobe activator is injected from the inlet apart from water injection well 220m.
(8) statistics of field test results and analysis
Block comprehensive water cut drops to 74.5% by 89% after field test, aqueous to reduce by 14.5 percentage points, increasing Produce crude oil 5.59 × 104T improves recovery ratio 21.7%, input-output ratio 1:13.2, field test results are good.

Claims (6)

1. a kind of method regulated and controled with endogenous microbes group of recovering the oil, which is characterized in that specifically include following steps, but be not limited to Following steps:
(1) screening of oil reservoir is tested
It is necessary to meet following condition for the screening of experiment oil reservoir:90 DEG C of reservoir temperature <, reservoir pressure < 20MPa, permeability > 100 ×10-3μm2, reservoir formation water salinity < 200000mg/L and Reservoir Crude Oil viscosity < 50000mPas;
(2) determination of experimental simulation core parameters
Experimental simulation core parameters include:Rock core length, diameter and sample point;
Experimental simulation rock core length:It is 100-200 that the distance between oil reservoir oil-water well, which is tested, with experimental simulation rock core length ratio: 1;Experimental simulation core diameter:It is 50-80 to test reservoir thickness and experimental simulation core diameter ratio:1;Experimental simulation rock core takes Sampling point:Sample point quantity is that a sample point is arranged at interval of 0.1m-0.2m, and sample point is evenly distributed on experimental simulation rock core On;
(3) physical simulation experiment of oil reservoir is tested
Using above-mentioned experimental simulation rock core carry out experiment oil reservoir physical simulation experiment, experiment the specific steps are:It loads and tests The identical experimental simulation rock core of Reservoir Permeability;Simulation core vacuumizes, the water flooding of saturation testing oil reservoir;Saturation testing oil reservoir Dehydration degassed crude;Experimental simulation rock core places 10d under experiment reservoir temperature and pressure condition, then carries out a water It drives, a water drive is extremely aqueous consistent with experiment oil reservoir current composite;Experimental simulation boring sample point is sampled, each sample point Sampling amount is 10-20mL;Aerobic, the facultative aerobic and anaerobe content of test sample;
(4) in experimental simulation rock core microbiologic population's regularity of distribution determination
According to above-mentioned test result, aerobic, facultative aerobic and anaerobe the regularity of distribution in experimental simulation rock core is analyzed, really Set oxygen and facultative aerobic, the facultative aerobic separation with anaerobe;
(5) determination of microbiologic population's regularity of distribution in oil reservoir is tested
Aerobic and facultative aerobic, the facultative aerobic separation with anaerobe, and experiment oil determined according to above-mentioned steps Hide the ratio of the distance between oil-water well with experimental simulation rock core length, determine respectively in experiment oil reservoir it is aerobic with it is facultative aerobic Separation and water injection well distance L1, facultative aerobic separation and water injection well distance L with anaerobe2
(6) determination of activator injection amount
Activator includes aerobic microbiological activator, facultative aerobic microbiological activator and anaerobe activator;
(7) determination of activator scene injection technology
Activator scene injection technology be in the experiment oil reservoir determined according to above-mentioned steps it is aerobic with it is facultative aerobic and facultative good Facultative aerobic and anaerobe activator inlet is respectively set at oxygen position corresponding with the separation of anaerobe, Facultative aerobic and anaerobe activator is injected from above-mentioned inlet respectively, note of the aerobic microbiological activator from experiment oil reservoir It is injected in well;
(8) field test and effect assessment
Field test is carried out according to above-mentioned determining activator injection amount and activator scene injection technology, is carried out after the test The statistics of field test results and analysis calculate the raising recovery ratio value and input-output ratio of experiment oil reservoir.
2. method according to claim 1 that regulated and controled with endogenous microbes group of recovering the oil, which is characterized in that described is aerobic Microorganism includes bacillus subtilis, pseudomonas aeruginosa and acinetobacter calcoaceticus, and facultative aerobic microbiological includes ground bacillus, oil Bacillus and achromobacter, anaerobe include methanogen, nitrate reduction bacterium and anaerobism dialister bacterium.
3. method according to claim 1 or 2 that regulated and controled with endogenous microbes group of recovering the oil, which is characterized in that described Aerobic microbiological activator is starch 1.5-2.0wt%, peptone 0.9-1.2wt%, dipotassium hydrogen phosphate 0.3-0.6wt%, double Oxygen water 1.0-1.5wt%, facultative aerobic microbiological activator are glucose 1.8-2.2wt%, Dried Corn Steep Liquor Powder 1.0- 1.4wt%, disodium hydrogen phosphate 0.4-0.8wt%, anaerobe activator are starch 1.5-2.0wt%, Dried Corn Steep Liquor Powder 0.5-0.8wt%, dihydrogen phosphate 0.3-0.6wt%.
4. method according to claim 1 that regulated and controled with endogenous microbes group of recovering the oil, which is characterized in that described is aerobic The determination of microorganism activator injection amount is as follows:
V1=R2L1Фβ1
In formula:V1- aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness, m;
L1- aerobic at a distance from facultative aerobic separation and water injection well, m;
The porosity of Ф-experiment oil reservoir, dimensionless;
β1- use level coefficient, dimensionless, value range are 0.5~0.6.
5. method according to claim 1 or 4 that regulated and controled with endogenous microbes group of recovering the oil, which is characterized in that described The determination of facultative aerobic microbiological activator injection amount is as follows:
V2=R2(L2-L1)Фβ2
In formula:V2- facultative aerobic microbiological activator injection amount, m3
R-experiment reservoir thickness, m;
L1- aerobic at a distance from facultative aerobic separation and water injection well, m;
L2At a distance from-facultative aerobic separation and water injection well with anaerobe, m;
Ф-reservoir pore degree, dimensionless;
β2- use level coefficient, dimensionless, value range are 0.8~1.0.
6. method according to claim 5 that regulated and controled with endogenous microbes group of recovering the oil, which is characterized in that the anaerobism The determination of microorganism activator injection amount is as follows:
V3=R2(L-L2)Фβ3
In formula:V3- anaerobe activator injection amount, m3
R-experiment reservoir thickness, m;
L-experiment oil reservoir injection well is at a distance from oil well, m;
L2At a distance from-facultative aerobic separation and water injection well with anaerobe, m;
Ф-reservoir pore degree, dimensionless;
β3- use level coefficient, dimensionless, value range are 0.6~0.8.
CN201810481543.8A 2018-05-18 2018-05-18 Method for regulating and controlling endogenous microbial community for oil extraction Active CN108716391B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810481543.8A CN108716391B (en) 2018-05-18 2018-05-18 Method for regulating and controlling endogenous microbial community for oil extraction

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810481543.8A CN108716391B (en) 2018-05-18 2018-05-18 Method for regulating and controlling endogenous microbial community for oil extraction

Publications (2)

Publication Number Publication Date
CN108716391A true CN108716391A (en) 2018-10-30
CN108716391B CN108716391B (en) 2021-04-06

Family

ID=63899966

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810481543.8A Active CN108716391B (en) 2018-05-18 2018-05-18 Method for regulating and controlling endogenous microbial community for oil extraction

Country Status (1)

Country Link
CN (1) CN108716391B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114427402A (en) * 2020-09-22 2022-05-03 中国石油化工股份有限公司 Method for improving recovery ratio by regulating and controlling microbial flooding oil reservoir
CN114427391A (en) * 2020-09-21 2022-05-03 中国石油化工股份有限公司 Method for removing stratum adsorption retention polymer by using microorganisms

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014018789A1 (en) * 2012-07-25 2014-01-30 Luca Technologies, Llc Enhancing energy recovery from subterranean hydrocarbon bearing formations using hydraulic fracturing
US8746334B2 (en) * 2011-12-07 2014-06-10 Husky Oil Operations Limited Microbial enhanced oil recovery process for heavy oil accumulations
CN104453811A (en) * 2014-10-27 2015-03-25 中国石油化工股份有限公司 Microbial enhanced oil recovering method of moderate-high permeability reservoir
CN104481476A (en) * 2014-10-27 2015-04-01 中国石油化工股份有限公司 Method for improving oil recovery efficiency through microbial oil displacement
CN105201474A (en) * 2015-10-23 2015-12-30 中国石油化工股份有限公司 Method for improving recovery ratio of indigenous microbial enhanced oil recovery
CN107965313A (en) * 2016-10-18 2018-04-27 中国石油化工股份有限公司 A kind of method for improving endogenous microbes displacement of reservoir oil field test results

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8746334B2 (en) * 2011-12-07 2014-06-10 Husky Oil Operations Limited Microbial enhanced oil recovery process for heavy oil accumulations
WO2014018789A1 (en) * 2012-07-25 2014-01-30 Luca Technologies, Llc Enhancing energy recovery from subterranean hydrocarbon bearing formations using hydraulic fracturing
CN104453811A (en) * 2014-10-27 2015-03-25 中国石油化工股份有限公司 Microbial enhanced oil recovering method of moderate-high permeability reservoir
CN104481476A (en) * 2014-10-27 2015-04-01 中国石油化工股份有限公司 Method for improving oil recovery efficiency through microbial oil displacement
CN105201474A (en) * 2015-10-23 2015-12-30 中国石油化工股份有限公司 Method for improving recovery ratio of indigenous microbial enhanced oil recovery
CN107965313A (en) * 2016-10-18 2018-04-27 中国石油化工股份有限公司 A kind of method for improving endogenous microbes displacement of reservoir oil field test results

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114427391A (en) * 2020-09-21 2022-05-03 中国石油化工股份有限公司 Method for removing stratum adsorption retention polymer by using microorganisms
CN114427391B (en) * 2020-09-21 2024-03-22 中国石油化工股份有限公司 Method for removing polymer retained by stratum adsorption by utilizing microorganisms
CN114427402A (en) * 2020-09-22 2022-05-03 中国石油化工股份有限公司 Method for improving recovery ratio by regulating and controlling microbial flooding oil reservoir
CN114427402B (en) * 2020-09-22 2024-02-06 中国石油化工股份有限公司 Method for improving recovery ratio by regulating and controlling microbial oil displacement reservoir

Also Published As

Publication number Publication date
CN108716391B (en) 2021-04-06

Similar Documents

Publication Publication Date Title
CN101988380B (en) Method for constructing oil reservoir oil displacement microbial community to improve crude oil recovery ratio
Bassin et al. Development of aerobic granular sludge under tropical climate conditions: the key role of inoculum adaptation under reduced sludge washout for stable granulation
CN101818634B (en) Method for regulating and controlling microbial community for oil extraction
CN103291267A (en) Method for improving oil well yields by means of oil pool indigenous microorganisms
CN108716391A (en) A method of it recovers the oil and is regulated and controled with endogenous microbes group
Ding et al. Effect of supplying a carbon extracting solution on denitrification in horizontal subsurface flow constructed wetlands
NZ598775A (en) Substrate-selective co-fermentation process
CN110593834A (en) Dominant regulation and control oil displacement method for internal and external source functional bacteria
Ruriani et al. Yeast isolation for bioethanol production
CN105201472A (en) Oil deposit stratal microflora regulation and control method
CN107965313A (en) A kind of method for improving endogenous microbes displacement of reservoir oil field test results
Wu et al. Dynamics and function of intracellular carbohydrate in activated sludge performing enhanced biological phosphorus removal
CN102168049B (en) Bacterial strain for producing gel breaking enzyme and application thereof
Navaratnam et al. Channelling of glucose by methanol for citric acid production from Aspergillus niger
CN102425398A (en) Produced fluid circulating treatment method for microbial flooding
CN103289936B (en) Method for producing biological de-emulsifying bacteria by using surplus sludge ultrasonic extracting solution
CN107558954A (en) A kind of method of high temperature and high salt high-content wax oil well microbial wax control
CN112796720A (en) Method for improving recovery ratio of low-permeability reservoir by applying microorganisms
CN1231655C (en) Biological process oil extraction method for prolonging period of validity by use of microbe to drive oil
CN114427405B (en) Regulation and control method for endogenous microorganism oil displacement
Suleiman et al. Enrichment of anaerobic heterotrophic thermophiles from four Azorean hot springs revealed different community composition and genera abundances using recalcitrant substrates
Buyondo et al. Unstructured kinetic modeling of batch production of lactic acid from hemicellulosic sugars
CN114427402B (en) Method for improving recovery ratio by regulating and controlling microbial oil displacement reservoir
CN115505736B (en) Method for bioleaching ionic rare earth ore in neutral or near-neutral environment
CN110939419A (en) Method for improving recovery ratio by efficiently mutagenizing endogenous microorganisms of oil reservoir

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Zhang Zonglin

Inventor after: Li Caifeng

Inventor after: Gao Guangjun

Inventor after: Guo Liaoyuan

Inventor after: Sun Gangzheng

Inventor after: Wang Lushan

Inventor after: Shu Qinglin

Inventor after: Liu Tao

Inventor after: Cao Yanbin

Inventor after: Song Yongting

Inventor after: Huang Gaojian

Inventor after: Feng Yun

Inventor after: Hu Jing

Inventor before: Shu Qinglin

Inventor before: Sun Gangzheng

Inventor before: Liu Tao

Inventor before: Cao Yanbin

Inventor before: Song Yongting

Inventor before: Feng Yun

Inventor before: Hu Jing

Inventor before: Li Caifeng

Inventor before: Gao Guangjun

Inventor before: Guo Liaoyuan

GR01 Patent grant
GR01 Patent grant