IPC classes for russian patent Method of development of heterogeneous-layer oil deposits. RU patent 2508446. (RU 2508446):
Another patents in same IPC classes:
Method of submerged reservoirs processing / 2507387
Method of processing for dissolution of acid-soluble material and solubilisation of hydrocarbons, emulsions and water barriers comprises the following jobs. Injection of micellar dispersion in the bed, said dispersion is a Winsor micro emulsion IV containing water, one or several precursors of organic acids, one or several surfactants and, not necessarily, one or several substances selected from salts, auxiliary surfactants and/or organic fluids which are not precursors of organic acids. Solubilisation is performed of micellar dispersion of hydrocarbons, emulsions or water barriers present in the bed and in-situ hydrolysis of, at least, a portion of organic acid precursor to produce sufficient amount of organic acid to cause notable dissolution of acid-soluble material present in filtration crests or nearby them, or other damage in the bed. Hydrolysis of organic acid precursor brings about the production of at least one of formic, acetic, hydroxiacetic and lactic acids. Organic acid precursor concentration makes at least 1 wt %. Well shutdown after introduction of micellar dispersion makes 0.5 h or more.
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Development method of bottom-hole zone / 2506422
Invention relates to oil industry. Method of bottom-hole zone treatment includes running-in of pipe string with packer to perforated interval, washing of the well equipped with master and casing valves, packer seating above the formation and treatment of the well by pumping of hydrochloric acid solution through the pipe string in pulsed mode, process exposure for reaction and extraction of reaction products. Optimal intake of the formation is set before treatment of bottom-hole zone. Then the pipe string at the well mouth below packer is equipped with impulse liquid pulsator, at that a valve is mounted between the packer and liquid pulsator. The pipe string is run-in into the well so that packer is located above the formation, thereafter with open master and casing valves the well is flushed by straight ring circulation during 10-20 minutes. The casing valve is closed and process liquid is pumped into the formation under pressure that does not exceed permitted pressure to the production string during 5-10 minutes. The casing valve is closed and process liquid is drained from the well. Washing and drainage of process liquid is repeated 3-5 times. Then hydrocarbon solvent is pumped to the pipe string, the packer is seated, hydrocarbon solvent is pressed into the formation by process fluid under pressure not exceeding permitted pressure to the formation; the well is subjected to process exposure. When process exposure is completed the valve is actuated, liquid pulsator is cut off, the packer is released, the pipe string is run-in additionally so that radial openings of the valve are located opposite the formation; and then the well is washed out by process liquid at open master and casing valves by straight ring circulation during 2 hours. At that casing valve is closed partially periodically till bottom hole pressure increases per 3-5 MPa in comparison with the initial pressure value transparent liquid appears; at that permitted pressure for production string is not exceeded. Thereafter hydrochloride acid solution and acid-clay cut mud heated up to temperature of 40-50°C is pumped to the pipe string, the packer is seated, hydrochloride acid solution and acid-clay cut mud are pressed to the formation by process liquid under pressure that does not exceed permitted pressure on formation, the packer is released and the well remains under exposure, then by return ring circulation reaction products are washed out till transparent liquid appears, hereupon actual intake of the formation is defined.
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Development method of bottom-hole zone / 2506421
Invention relates to oil industry. Method of bottom-hole zone treatment includes running-in of pipe string with packer to perforated interval, washing of the well, packer seating in production casing with master and casing valves above the formation and pumping of hydrochloric acid solution through the pipe string in pulsed mode, process exposure for reaction and extraction of reaction products. Optimal intake of the formation is set before treatment of bottom-hole zone. At the well mouth the pipe string below packer is equipped with impulse liquid pulsator, at that a valve is mounted between the packer and liquid pulsator; pipe string is run-in into the well so that packer is located above the formation; thereafter the well is flushed with process liquid at open master and casing valves by straight ring circulation in pulse mode during 10-20 minutes. The casing valve is closed and process liquid is pumped into the formation under pressure that does not exceed permitted pressure to the production string during 5-10 minutes. The casing valve is closed and process liquid is drained from the well. Washing and drainage of process liquid is repeated 3-5 times. Then actual intake of the formation is determined at pressure that does exceed permitted pressure to the production string. If actual intake is lower than the optimal one then hydrochloride acid bath is installed in the well opposite formation interval under pressure that does not exceed permitted pressure to the production string. If actual intake is equal to the optimal one or higher then hydrocarbon solvent is pumped to the pipe string, add process liquid up to volume bigger per 0.5-1 m3 than volume of the reagent displaced from the pipe string under pressure not exceeding permitted pressure to the formation. The well is subjected to process exposure. When exposure is completed the valve is actuated, liquid pulsator is cut off, the packer is released, the pipe string is run-in additionally so that radial openings of the valve are located opposite the formation; by return ring circulation reaction products are washed out during 3-5 hours, at that fluid influx from the formation is controlled. Then casing valve is closed and by process liquid pumping to the pipe string through the valve well intake is determined under intake pressure of the formation.
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Oil-field biocide made from peracetic acid and method for use thereof / 2506300
Invention relates to biocide compositions for aqueous fluid agents used in oil- and gas-field operations. The biocidal composition of the aqueous fluid medium for treating wells contains a polymer or a copolymer for modifying viscosity of the fluid medium, a monocarboxylic peracid in an antimicrobial amount ranging from about 1 ppm to about 1000 ppm, and hydrogen peroxide in a concentration lower than that of the peracid in an aqueous medium. Said composition, containing a polymer or copolymer, reduces viscosity of the fluid medium, reduces friction or increases viscosity, and the acid is a precursor. The method of providing biocidal activity in the well treatment fluid medium involves adding to the well treatment fluid medium said composition which contains a polymer or copolymer to modify viscosity and feeding said medium into the underground medium. The invention is developed in subclaims.
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Addition of non-ionic surfactants to water soluble block copolymers to increase stability of copolymers in aqueous solutions containing salt and/or surfactants / 2506299
Invention relates to extraction of hydrocarbons from underground formations. An aqueous composition containing a mixture of water, about 0.05-10 wt % of the total weight of at least one water-soluble block copolymer, containing: at least one block which is water-soluble by nature, which contains at least 34 wt % hydrophilic links relative the total number of links of the water-soluble block, and containing hydrophobic links and at least one hydrophobic block containing 67 wt % hydrophobic links relative the total number of links of the hydrophobic block, about 0.01-10 wt % of the total weight of a non-ionic surfactant with HLB value ranging from 1 to 12, and about 0.1-20 wt % of the total weight of at least one inorganic salt. The method of extracting hydrocarbons from underground formations involves feeding an aqueous fluid containing said composition into the formation. The method of forming cracks in an underground formation surrounding a well bore involves a step of feeding a fluid containing said composition into the well for hydraulic fracturing.
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Oil deposit development method / 2502864
As per an oil deposit development method involving pumping of fringe of biological surface active substance bioSAS KShAS-M and hydrocarbon solvent, first, aluminosilicate composition based on 11% of hydrochloric acid solution is pumped; in addition, fringe contains oil and formation water, and isooctane as a solvent; with that, fringe contains the following, %: formation water 54-88, bioSAS KShAS-M 1-2, isooctane 1-4, and oil 10-40.
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Development method of high-viscosity oil deposit / 2501941
Development method of a high-viscosity oil deposit involves drilling of a deposit with vertical production and injection wells, pumping of heat carrier through an injection well and cyclically through production wells, extraction of products through production wells after heat carrier pumping is stopped and exposure is completed, and conversion of the next production well for heat carrier pumping. Drilling of the deposit and pumping of heat carrier is performed to an oil-bearing formation, and priority of conversion of production wells for pumping of heat carrier is determined as per the least oil productivity and bottom-hole temperature. At the first stage, drainage of bottom-hole zones is performed, which consists in alternating operations of heat carrier (steam) pumping, exposure and extraction of the product. At the second stage, heat carrier (hot water) is pumped to injection wells at the temperature of 60-100°C and from time to time a solvent is pumped in the amount of 0.1-1% of the volume of pumped hot water with surface active substance in the amount of 0.1-2% of the solvent volume; hot water is pumped to production wells in the first cycle in the volume equal to the volume of extracted liquid after the last steam heat treatment, and volumes of the following pumping operations are equal to volumes of extracted liquid in the previous cycles; before hot water is injected to production wells, a solvent bank with surface active substance in the amount of 0.1-2% of the solvent volume is pumped in each cycle; volume of solvent bank is calculated. Liquid fraction of pyrolysis of automobile tyres is used as a solvent.
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Emulsion-stabilising agents to be used in fluid media for drilling and completion of wells / 2501829
Stabilised emulsion composition includes oily fluid medium, fluid medium being at least partially non-mixed with oily fluid medium, and emulsion-stabilising agent containing the first ionic compound soluble in oily fluid medium or the above fluid medium, and the second ionic compound with a charge with an opposite sign relative to the first ionic compound. The proposed method involves production of the above composition of stabilised emulsion and its placement into an underground formation as a part of underground work. The method involves production of the above composition and drilling of a well in the underground formation using it. The method for obtaining the above composition involves the following: production of oily fluid medium; production of the above fluid medium; production of emulsion-stabilising agent including the first ionic compound, which is soluble in oily fluid medium or the above fluid medium, and the second ionic compound with the charge with opposite sign relative to the first ionic compound, and combination of oily fluid medium, fluid medium and stabilising agent with formation of composition.
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Method of secondary oil extraction / 2499135
Proposed method comprises injection of 0.1-100000 ppm of amine alkyl phosphonic acid to the system of reservoir, said acid being selected from the group of compounds combined with amine neutraliser selected from special group of compounds provided that amine neutraliser represents the combination of at least two structurally different amine types. Note here that first one is hydrophobic type with hydrophilic-lipophilic balance smaller by at least two units than hydrophilic-lipophilic balance of the second one. Said first and second amine types are used in equivalent ratios (first one is more hydrophobic): second (more hydrophilic) n the range of 10:1 to 2:5.
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Oil pool development method / 2244110
Invention provides a method of developing oil pool allowing production of oil from water-rich oil reservoir under difficult geological-tectonic conditions in the last development stage. In the method, neutral salt of carbonic acid and acid solution are forced into formation through injecting well with water generated in gas-liquid fringe created in formation. After pumping of neutral salt of carbonic acid, acid solution is pumped by portions alternating with water pumping. Before pumping of acid solution portions beginning by at least second portion, selective insulation of high-permeable formation intervals is performed. Aforesaid neutral salt of carbonic acid utilized is sodium carbonate aqueous solution or aqueous suspension of calcium carbonate and aforesaid acid solution is aqueous hydrochloric acid solution. Selective insulation of high-permeable formation intervals involves use of freshly prepared controllable viscoelastic composition containing water-soluble acrylic polymer, cross-linking agent, thermal stabilizer, surfactant, and water. Summary concentration of acid solution is determined from concentration of neutral salt of carbonic acid on the base of stoichiometric proportions.
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Method of treating bottom zone of low-permeable oil reservoirs / 2244111
Invention aims at increasing productivity of oil- and gas-producing and injecting wells exposing high-temperature low-permeable oil reservoirs. In the treatment method according to invention including forcing enzyme substrate and separate enzyme into formation and creating conditions to enzymatically convert substrate into acid, geologic and productive characteristics for each interval of bottom zone are determined in order to pick out low-permeable intervals of oil reservoir for treatment, whereupon properties of enzyme substrate and separate enzyme as well as conditions for their pumping are chosen. Substrate utilized in the method is head fraction of methyl- and/or ethyl-, and/or butyl acetate production, to which aliphatic alcohols are added, and enzyme is an acid solution. Substrate is pumped simultaneously and/or before, and/or after pumping of enzyme, after which well is closed for some time and then opened and placed under predetermined operational conditions.
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Oil recovery composition / 2244809
Invention is intended for use during development of oil pools at different waterflooding phase for intensifying functioning of producing wells and increasing current oil recovery of formation. Composition contains, wt %: liquid hydrocarbon 10.0-20.0, oil-soluble surfactant 0.3-5.0, water-soluble or water-oil-soluble surfactant 0.1-1.0, superfine hydrophobic material 0.1-2.0, and water (the rest). Composition may further contain 0.3-5.0% calcium chloride. Oil recovery is increased owing to hydrophobization of formation structure, reduction of surface tension in water/rock/oil phase boundary, increase in detergent power of polluted surface, increase in composition viscosity, and increase of relative permeability of the formation for hydrocarbon phase as compared with water phase.
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Formation bottom area treatment composition / 2244810
Composition contains 0.05-2.5% of hydrophobic power, 0.05-10% of ethylene/vinyl acetate copolymer, and organic solvent. Composition intensifies oil production owing to increased effective radius of formation bottom area treatment, prevention of moistening inversion effect upon fall of hydrophobic agent concentration, and, consequently, decreased volume of simultaneously produced water.
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Method for extracting hydrocarbons deposits / 2244811
Method includes drilling product and force wells, forcing gas and water through force wells into separate zones of productive bed and extraction of hydrocarbons from product wells, forming separate gas, water and hydrocarbon saturated areas with major contents of respectively gas, collected therein for later use, water and hydrocarbons, periodical pumping of collected gas from formed gas saturated zones to water saturated zones, periodical pumping of water to gas saturated zones is performed. It is possible to pump collected gas to water saturated zones in form of gas-water mixture. It is possible to pump in passing gas of current deposit. It is possible to pump hydrocarbon or non-hydrocarbon gas from other sources. It is possible to pump water with admixture of specifically selected chemical reagents or compositions thereof. When gas content in water saturated zones reaches from 0.1 to 28% from water content in water saturated zones it is reasonable to generate resilient waves with frequency within range from 0.0001 to 45 KHz and amplitude within range from 0.02 to 2.8 MPa. It is reasonable to pump gas and water to separate areas of productive bed with concurrent generation of resilient waves in there with frequency within range from 0.0001 to 45 KHz and amplitude within limits from 0.02 to 2.8 MPa.
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Method for oil bed extraction / 2244812
Method includes pumping of Sulfacella water dispersion into bed through force well and extraction of oil through extracting well, said dispersion additionally containing non-ionogenic surfactant AF9-12 with following ratio of components, in percents of mass: Sulfacella 0.5-1, AF9-12 0.01-0.1, water- the rest, while, before pumping of said dispersion mineralized water is pumped with total mineralization until 290 g/l in amount of 10% from volume of said dispersion, when pumping said dispersion prepared in fresh water, drain water is previously pumped, and when pumping said dispersion made from drain or bed water, bed water is previously pumped. For preparation of said dispersion fresh, drain or bed water is used with mineralization till 290 g/l.
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Method for operation of gas-condensate deposit / 2245997
Method includes examination of operation well for gas-condensation and periodical cleaning of face-adjacent well area from precipitating hydrocarbon condensate by pumping hydrocarbon condensate solvent into bed, exposure of well for period of condensate dissolution and following removal of received solution from face-adjacent area during well launch, as solvent binary mixture is used with unlimited mutual solubility of components, while at least one of them has unlimited mutual solubility with hydrocarbon condensate, and relation of binary mixture components is determined from previously built phase diagram of three-component system, formed during dissolution of hydrocarbon condensate. As binary mixture with unlimited mutual solubility of components a mixture of acetone and methanol is used, or chloroform and methanol, or chloroform and aniline, or chloroform and acetone.
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Method for preserving collecting properties of face-adjacent area of productive bed of oil-extractive well / 2245998
Method includes placing water solution of carnallite ore, either modified, concentrated, or mixtures thereof, said solution is used at maximal for well temperature conditions concentration and is pumped in amount, necessary and enough for forming a hydraulic column in well shaft above ceiling of productive bed and along remaining shaft height well is filled with water up to mouth. Carnallite ore used has composition, in percents of mass: potassium chloride 20.5-21.5; sodium chloride 19.5-22.5; magnesium chloride 24.0-27.0; crystallization water 29.5-30.5. Modified ore has composition, in percents of mass: potassium chloride 23.0-29.5; magnesium chloride 31.8-46.0; crystallization water - the rest. Said water solution is prepared by dissolving ore in fresh technical water, drained from oil preparation plants, or in bed water. In case of dissolving in bed water, the latter is pumped from well at temperature 60-90°C. During perforation of well, value of technological liquid hydraulic column above productive bed ceiling is taken equal to (1.03-1.07)-(1.05-1.1)Pb, where Pb - productive bed pressure. Water solution of carnallite ore is used at density 1.23-1.37 t/m3. During use of said solution as working body of force wells it is used at density 1.05-1.20 t/m3, and solution also contains swelling inhibitor for argillaceous component of oil and gas bearing bed, like oxyethylenedendiphosphone acid, in amount 0.05-0.15% of used dissolved ore mass.
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Oil extraction method / 2247231
Method includes treatment of face area of oil bed by hydrophobic agent in organic solvent and pressing oil from collector with following delivery of oil from face area of product well for treatment of oil terrigenic bed, in form of hydrophobic agent solution of ethylene copolymer with vinylacetate in ethylbenzol or fraction thereof is used in relation 1:1 - 10, treatment of face area is performed with following ratio of components, in percents of mass: ethylene copolymer with vinylacetate 0.05-2.0, ethylbenzol or fraction 0.05-20.0, organic solvent - the rest.
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Coal processing method / 2248398
Coal is affected by methanogenic consortium of microorganisms with culture medium utilizing continuous pumping of culture medium through wells and tank wherein methanogenic consortium of microorganisms with culture medium is placed. Tank is installed on the surface above wells and pumping of culture medium from the bottom of tank through methanogenic consortium of microorganisms. Process produces biogas and coal-water fuel.
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FIELD: oil-and-gas industry.
SUBSTANCE: proposed method comprises injection of working agent via injection wells, extraction of oil via production wells, injection of sealing agent based on sodium silicate and acid into injection or production wells, holding the welds for a day and making them operate. Prior to injecting said sealing agent into bed, water-slug is injected in amount inhibiting the mixing of bed water with sealing agent till its gelation but not smaller than one volume of tubing. Holding is performed after injection of said agent into the bed. Sealing agent is composed by gel-like compound of the following composition, wt %: sodium silicate - 3-8, sulfonic acid - 0.38-1.5, chromium acetate - 0.35-0.9, monoethanol-amine - 0.35-0.9.
EFFECT: higher efficiency of sealing.
2 ex, 1 dwg
The invention relates to the oil and gas industry, in particular to methods of oil production from inhomogeneous watered formations at the late stage of development of oil fields.
There is a method of selective isolation of water inflow into the oil wells, providing for the pumping of water soluble acrylic series [kleschenko I.I., A.V. Grigoriev, A.P. Insulation work during completion and operation of wells. - M Nedra, p.31]. Isolation mechanism of formation waters based on the interaction of acrylic polymers with salts formation waters or adsorption of polymers on the breed. However, this method is applicable only if the isolation of formation of highly mineralized water chlorine-calcium type.
There is a method of limitation of water flow into the well, including sequential injection of an aqueous solution of sodium silicate and hardener - [SU, №1423726, 21 33/12, 1988]. The aqueous solution of sodium silicate reacts with the hardener - solution of hydrochloric acid, as a result of which produces high-viscosity gel, which then turns the substance - , pores.
The disadvantages of this method is, that in the process of injection is prematurely and uneven mixture injected solutions, with the formation of blocking the screen near the discharge line, and even in the well bore. In the result, the composition does not reach the destination and not achieved wide coverage of the flooded areas of the reservoir.
The closest analogue of the invention is a way to develop a layered inhomogeneous oil fields (Russia, №2128768, 21 43/22, 1999), applied at processing of bottom-hole zones extractive or injection wells to water influx isolation in production wells and alignment of injectivity of wells, as well as with isolation of cross-flows in wells and the liquidation of old wells. By way inject the insulating agent through injection wells, select oil through production wells. In flooding of production wells wells pumped insulating agent on the basis of silicate of sodium and hydrochloric acid. Well kept for the day and start in work.
The disadvantage of a low efficiency of insulation, short time of gelling, low strength (30) and the risk of precipitation of salts of silicic acid at a meeting gel-forming composition with highly mineralized stratal waters.
In the invention solved the technical problem of improving the efficiency of isolation due to the increased time of gelling, increase the strength of the gel.
The task is solved by a how to develop layered inhomogeneous oil fields, including the injection of the agent through injection wells, selection of oil through production wells, injection, injection or producing wells in flooding wells isolation agent on the basis of silicate of sodium and acid, extract of wells during the day and run them in the work, according to the invention before the injection isolation agent into the reservoir, pump fresh water in a volume that provides produced water with insulating agent before the time of his , but not less than one volume of tubing, the shutter speed is carried out after the agent in the formation, and as an isolation agent use composition in the following composition, mass%:
Sodium silicate 3-8
Sulfamic acid 0,38-1,5
Chromium acetate 0,35-0,9
Monoethanolamine 1,5-2,5 Water rest
Thus, the proposed method differs from analogue novelty composition and method of injection of the composition to the formation. The additional introduction of chromium acetate acid-gel-forming system (sodium silicate + sulfamic acid) leads to further strengthening of the system. This happens due to the formation of complexes between negatively charged silicate ions and cation of chromium in three dimensions. Thus gel is formed by hydrogen bonds with silicic acid, strengthens spatial silicate complexes.
In addition, the difference between a prototype and a novelty of the method is the method of injection, which consists in preliminary downloading of the reservoir rim of fresh water to push mineralized stratal waters to prevent precipitation of the reaction of metal salts with silicate ions according to the scheme:
Na 2 Si 3 O 7 +CaCl 2 =CaSi 3 O 7 |+2NaCl
Na 2 Si 3 O 7 +MgCl 2 =MgSi 3 O 7 |+2NaCl
Volume rim of fresh water are selected so that the while pushing through the layer of insulating agent, due to the formation of «languages», and the composition is not mingling would mineralized formation water up to the end of the term of gelation. For this volume rim of fresh water are at least one volume of tubing, the higher the volume, the better the resulting insulating effect.
To determine the optimal ratio of reagents, experiments were conducted with different proportions of components.
Used sodium silicate powder, dried in a spray drier plant OJSC tanning agent» with the module 2,95. Sulfamic acid (NAO) was used 15%concentration density 1,083 g/cm 3
Chromium acetate (AX) used in the form of 10%solution with density 1,039 g/cm 3 .
Monoethanolamine (MEA) used in the commodity undiluted form.
Mainly studies were conducted with isolating agents, containing in its composition 5-7% sodium silicate, which is obtained sufficient strength gel (1000-7000 PA) at the required time (10-20 hours).
The results of the laboratory work graphs of the time dependence of the beginning of gel formation and strength of the received gel from sulfamic acid concentration (BAC) of figure 1.
As can be seen, with increasing content of the sulfamic acid in the solution, the strength of the isolation of the agent increases, and the start time of gelling decreases, therefore, to obtain a sufficiently strong gels with required time of gelling you must choose the optimum concentration of sulfamic acid, that is from 0.8% to 1.6% of the mass.
When the content of SAK more than 1.6% of the mass. dramatically reduces the time of gelling, although the strength is high. In reducing the number of SAK less than 0.8 gel formation is slow, but reduced strength characteristics.
As can be seen from the figure, compared with the prototype of the proposed composition of the gelation time is increased to 2.28 times, and strength increases in 230 times.
Thus, the goal of the project of the claimed invention is considered to be solved.
Example of the implementation of the proposed method on the producer. Well depth of 3500 meters, tubing launched 3250 m, the thickness of the productive formation of 2,5 m
Preparing to 25 m 3 of water isolation agent with the following composition: 6,4% sodium silicate, 0.7% of chromium acetate, 1,064% SAK, 2.5% of the IEA and 89, 366% water.
Originally tubing is served 25 m3 of fresh water. Following the fresh water is pumped 25 m 3 of water isolation agent (2,5 volume of tubing). Then in the tubing is served 10 m 3 fluid (which applies fresh water) and the previous volume of liquids is squeezed into the formation. Well the day is left to the solidification of the gel, then proceed to the process of development.
Example of the implementation of the proposed method on the discharge hole. Well depth of 3000 m, pipe discharge lowered to 2900 m, capacity of the receiving reservoir 1,5 m
Preparing 15 m 3 of water isolation agent containing 6,7% of the mass. sodium silicate, 0,82% of the mass. chromium acetate, 0.85% of sulfamic acid and 1.50% monoethanolamine and 90,13% water.
In the injection pipe originally served 20 m 3 rim of fresh water (two volumes of pipes, then pumped 15 m 3 of water isolation agent. The whole mixture is squeezed into the formation liquid (fresh water) in the amount of injection pipe 10 m 3 . Well it is left on 24 hours for «seizure», then resumed the work on discharge of water.
Application of the proposed method allows to successfully develop heterogeneous permeability, flooded deposits with simultaneous increase of the oil recovery ratio and reduce the water content of products.
Way to develop a layered inhomogeneous oil fields, including the injection of the agent through injection wells, selection of oil through production wells, injection, injection or producing wells in flooding wells isolation agent on the basis of silicate of sodium and acid, extract of wells during the day and putting them into operation, wherein the previously, before the injection isolation agent into the reservoir, pump fresh water in a volume that provides produced water with insulating agent before the time of his , but not less than the volume of tubing, the shutter speed is carried out after the agent in the reservoir, and as an isolation agent use composition of the following composition,% Mas.:
Sodium silicate 3-8
Sulfamic acid 0,38-1,5
Chromium acetate 0,35-0,9
Monoethanolamine 1,5-2,5 Water Rest
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