• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A process for recovering oil from an oil-bearing subterranean reservoir penetrated by at least one injection well and at least one production well which comprises the steps of: (1) injecting into the oil-bearing subterranean reservoir through the injection well a first injecting fluid consisting essentially of (a) 1% to 30% by weight of an internal olefin sulfonate having 10 to 26 carbon atoms and a disulfonate content of 20% by weight or less, (b) 0.1% to 20% by weight of a cosurfactant, and (c) a brine; (2) injecting, as a second injecting fluid, an aqueous polymer solution having a viscosity higher than that of the first injecting fluid into the oil-bearing subterranean reservoir; and (3) recovering oil replaced with the first and second injecting fluids through the production well. This process can recover oil from subterranean reservoirs at a high oil recovery efficiency without destroying a micro-emulsion during sweeping in the subterranean reservoir even when the salt concentration of the formation water is widely changed.
    公开号:SU1419527A3
    申请号:SU843728544
    申请日:1984-04-03
    公开日:1988-08-23
    发明作者:Укигаи Тосиюки；Хагивара Масааки；Ямада Дзунити
    申请人:Лион Корпорейшн (Фирма)；
    IPC主号:
    专利说明:

    Inventories refer to the oil-bearing oil reservoir, in particular, to the multilateral displacement of oil from the reservoir.
    The purpose of the invention is to increase the recovery of oil.
    The first HarHeTaRNfbie fluids used in the proposed method for extracting petroleum contain base olefins with internal unsaturated bonds (internal olefins sulfonates) with 10-26 carbon atoms, 20 May D or less disulfonate and co Surfactant.
    As internal olefin sulfonates, sulfonates obtained by sulfonating internal olefins containing as the main component of a vinylene mono-olefin with 10-26 carbon atoms, preferably 12-24 carbon atoms, and having the general formula
    R - CH CH - R,
    where R and R are, independently of one another, straight or branched chain hydrocarbon radicals having one or more carbon atoms, the total number of carbon atoms R and R being 8-24, preferably 10-22, and not necessarily containing about 33 wt.% (About a third part of olefins) or less monosolems of the trisubstituted type, followed by neutralization of the sulfonated products with appropriate alkalis and not necessarily with the hydrolysis of the neutralized products.
    The resulting sulphonates are internal olefins and usually contain about 10-60% by weight of double-alkenylsulfonates and about 90-40% by weight of hydroxyalkane sulfonates, and also contain about 80% by weight or more monosulfonates and about 20 wt.% or less disulfonates.
    In addition, sulfonates of internal olefins having a composition different from that described can be obtained by appropriate selection of the conditions for sulfonation and hydrolysis. An increase in the number of carbon atoms of the internal olefin leads to an increase in the com- position ratio of disulfonate
    The content of disulfonate in the sulfonates of internal olefins should
    0
    five
    0
    five
    0
    five
    0
    five
    0
    five
    be about 20 May, 7, or M (lower). If the disulfonate content is more than 20 wt.%, the surface tension at the oil-water interface does not decrease when the first injected fluid is injected and therefore the oil recovery efficiency decreases due to the relatively large surface tension at the interface of the microemulsion formed in the subterranean formation.Thus, a small amount of disulfonate in the internal olefin sulfonates increases resistance to salinization and resistance to changes in salt concentration in the formation water, impaired ability of internal olefin sulfonates, and reduced surface tension at the interface, whereby the content of disulfonates in internal olefin sulfonates is preferably about 0.5 to 15% by weight, more preferably about 1 to 12% by weight. %
    Internal olefin sulfonates may be alkali metal salts, alkaline earth metal salts, ammonium salts thereof, and organic amine salts. Desirable countercations are Na, K, Mg, NH and alkanolammonium.
    Examples of internal olefin sulfonates suitable for use in the invention are an internal olefin sulfonate having 12, 13, 14, 15. 16, 17, 18, 20, 22, 24, 12-16, 13-15, 14-16, 14-18, 15-18, 16-18, 16-20, 18-20 and 20-24 carbon atoms. These internal olefin sulfonates may be used alone or in a mixture in any combination.
    The amount of internal olefin sulfonates contained in the first injection fluid is preferably in the range of from 1 to 30% by weight, more preferably from 3 to 25% by weight. An inner olefin sulfonate content of less than about 1 wt.% Will not provide a large amount of the target microemulsion in subterranean formations due to dilution with formation water. This reduces the degree of oil recovery due to insufficient growth of moving oil zones in subterranean formations. Conversely, when the content of the internal olefin sulphonate is approximately more than 30% by weight, the process becomes
    u
    uneconomic due to the increase in the cost of internal olefin sulfonate, although the required moving oil zones are easily formed in subterranean formations.
    The first injected liquids also contain an auxiliary surfactant (co-surfactant) as the main constituent. These CO-surfactants, together with the sulfonates of internal olefins, form the required microemulsions in subterranean formations. Co-surfactants suitable for use in the invention have an alcoholic hydroxyl group.
    Desirable co-surfactants are alcohols having the general formula
    (CHjCH O) n H,
    where n is a number from O to about 4; an alkyl or alkenyl group having 3 to 8 carbon atoms when and an alkyl, alkenyl, phenyl or apkylphenyl group having 6 to 15 carbon atoms when. Aliphatic groups R may be straight chain or branched chain.
    Examples of such alcohols are butanols, pentanols, and hexanols ()
    The first injected fluids may contain about 0.1–20 wt.% Co-surfactant. However, the preferred concentration of co-surfactant in the first injected fluids is in the range of about 1-10 wt.% In terms of the formation of emulsions and a decrease in the surface tension at the interface.
    Since the first inspected liquids contain sulfonates of internal olefins as surfactants, they are characterized by excellent stability in saline and hard water, any aqueous media can be used to prepare the first injected liquids, including soft and hard water and brines with a high salt concentration. By priper, you can. Lightly use
    call rain, river, lake, formation and sea water. In relation to stability in hard water, a brine can be used containing a large amount of polyvalent metal ions (for example, about 5000 ppm Mg ion, i.e. about 2.6 wt.% Based on MgSO4). In addition, water (or brine) containing about 10% by weight of alkali metal salts (regardless of the type of alkali metal salts) may be used. In particular, when, in addition to the sulfonates of internal olefins, other surfactants are contained in the first injected liquid, or when appropriate co-surfactants are selected, a brine with an alkali metal salt concentration of about 15% by weight can be used.
    Thus, water (or brine) used to form the first injected fluids may contain about 0-15 wt.%, In the preferred embodiment, about 0.5 12 wt.% And most preferably, about 1-10 wt.% inorganic salts. Typical examples of salts contained in water (or brine) are
    NaCl, KCl, and K2S04. For example, seawater contains about 3.5 wt.% Inorganic salts, including about 1600 ppm, based on Mg, divalent metal ions. The salt concentration is within the preferred range of salt concentrations in water used in the proposed method.
    The first injected fluids may optionally contain other auxiliary surfactants together with internal olefin sulfonates. Examples of such auxiliary surfactants are anionic surfactants and nonionic surfactants, such as petroleum sulfonates, alkylbenzene sulfonates, polyoxyethylene etileialkilefirsulfaty, dialkilsul- fosuktsinaty, alpha-olefin sulfonates, paraffin sulfonates, soaps, higher alcohol ethoxylates, ethoxylates of alkylphenols, esters of polyhydric alcohols and fatty acids, fatty acid alkyl amides, and polypoxyethylenides and fatty acids.
    In addition, optional
    Ordinary loading substances can be used as an additive to the first injectable fluid, since the viscosity of this fluid is from
    very small. Examples of such loading materials are water-soluble polymeric substances used in the second proposed injected fluids and listed below. For this purpose, a small amount of oil (or oil) may also be added to the first liquid to be injected.
    The second injected fluids injected into the underground apast following the first injected fluids are an aqueous polymer solution having a higher viscosity than the viscosity of the first injected fluids. The water-soluble polymeric substances used as the second injected fluid are either natural or synthetic substances. Examples of such water soluble polymeric substances are microbial heteropolysaccharides, naphthalene sulfonic acid condensates - formaldehyde, polyacrylamides, polyacrylates, hydroxyethylcellulose and carboxymethylcellulose. The concentration of water-soluble polymeric substances in the second injected fluids is selected depending on, for example, the viscosity of the first and injected fluids and the types and molecular weights of the water-soluble polymeric substances. A suitable concentration is about 0.01-1% by weight.
    According to the proposed method, oil is extracted from subterranean formations, for example, injecting a first injected fluid into at least one injection well, and then a second injected fluid into the same base to extract oil from at least one productive well. A suitable amount of the first injection fluid injected into the injection well is about 3-25% of the pore volume of the subterranean formations.
    According to the proposed method, nicro emulsions are formed in subterranean formations and therefore, surfactant aqueous solutions that do not contain significant amounts of oil can be used as the first injected fluid. In accordance with the method of extracting oil has economic advantages due to the fact that it is not required to add oil to the underground
    276
    layer In addition, the proposed method belongs to the methods of micellar displacement and uses, as surfactants, sulfonates of internal olefins, which are resistant to salts and in hard water and form the required microemulsions that have a very low surface tension. oil is displaced from subterranean formations at the interface.
    As a result, it is easy to use as soft water, sea water. t to and reservoir water with a high concentration of salts. Microemulsions formed in subterranean formations are not significantly adversely affected by the inorganic salts present in the formation water. The micellar extrusion method can be easily applied to subterranean formations containing both low viscosity oil and high viscosity oil. A high degree of oil recovery can be achieved, since stable microemulsions are maintained in subterranean formations.
    Example 1. In a beaker, a weighed portion of the first injected liquid was prepared, consisting of 6.0% sodium sulfonates C, yC of internal olefins (i.e., YOS - Na) with a disulfonate content (DS) of 8% based on effective
    component as surfactant; 3.0% amyl alcohol as an auxiliary surfactant (CO-surfactant) and a 91% aqueous solution of sodium chloride containing 5% sodium chloride dissolved in demineralized water as brine. The resulting mixture was stirred at a speed of 100 rpm at 25 ° C.
    A second injected liquid was prepared by dissolving 1500 ppm (0.15%) xanthan gum in brine.
    To assess the ability to form a microemulsion of the sample in a soil column (core), an experiment was carried out using a Bury (Vegea) sandstone core measuring 3.8 cm in diameter and 7 cm in length, having a permeability of about 500 mD (millidarcy) and a porosity of about 20%.
    The core, thoroughly saturated with brine, was placed in the holder, and then fuel oil was pumped into the core under pressure at a rate of 6 until the brine stopped flowing. Behind
    . 7
    The brine was pumped under pressure at the same rate by the water displacement method until the oil content in the output stream was less than 0.1%. Thus extracted fuel oil from the core.
    After the process of displacing water into the core, a first injected liquid was injected under pressure with a flow rate of 0.1 in an amount of 15% of the pore volume, and then a second injected liquid was injected under pressure. consumption of 0.1 cm3 / min in the amount of 100% of the pore volume. After the injection of the first and second liquids and after soaking, 15 cm of liquid were obtained as a peevom outflow. As a result, a clean (or clear) microemulsion was obtained.
    Example 2. In a beaker, a portion of the first injected liquid was prepared, consisting of 6.0 C, j-Cp YOS-Na containing DS 8Z per effective component as a surfactant; 3.0% amyl alcohol as an auxiliary surfactant and 91% aqueous solution of sodium chloride, containing 5% sodium chloride, dissolved in demineralized water, as brine. The resulting mixture was transferred at a speed of 100 rpm for 10 minutes at YDS with different DS contents prepared by changing the molar ratio of the starting internal olefins and SO. in the sulfonation reaction.
    A second injection fluid was prepared by dissolving 1500 ppm xanthan gum in brine.
    The ability to form microemulsions, the ability of the resulting microemulsions to reduce surface tension and the interface and the efficiency in the extraction of oil. The first injected fluids were evaluated as follows.
    t
    The ability to form microemulsions was determined visually by mixing the sample and oil in a ratio of 5/3 and was designated O if the emulsion was formed, and X if the emulsion was not formed. The surface tensions were measured with a rotating droplet type ziometer at 71 ° C in a suitably diluted system.
    -
    19527®
    Experiments on the extraction of oil were performed using cores from Bury sandstone, having a size of 3.8 cm in di
    with a meter and 28 cm in length and permeability of about 00 mD, and a porosity of about 20%, as follows.
    The core, thoroughly saturated with brine, was set in the holder, and
    10 then the fuel oil was injected into the core under pressure at a flow rate of 6 cm / min until it ceased to exit the brine. Then, brine was injected under pressure with the same flow rate by the method of displacement with water until the content of fuel oil in the waste stream was less than 0.1%. Thus extracted fuel oil.
    After the process of water displacement
    20 carried out the method of micellar extrusion, for which the core holder and microemulsions were placed in a bath with a constant temperature of 71 C. First, the first were pumped under pressure
    25 injected liquids in the core with a flow rate of 2 feet / day (61 cm / day) in an amount of 152 of the pore volume, then under pressure in the core, a second injected fluid was injected with a flow rate
    30 2 feet / day (61 cm / day) in the amount of 100% of the pore volume and, finally, brine was injected into the core under pressure at a rate of 2 feet / day (61 cm / day) in the amount of 100% of the pore volume. Oil was thus extracted at once. The efficiency of oil recovery was determined by measuring the amount of water in the core after the aeotropic toluene study.
    40 Research results are shown in Table. one.
    In tab. 1 sample 1 is the proposed example, and samples 2 and 3 are comparative. Sample 2 is semi-someone whose same way as sample I, except that no surfactant was used in this case and the sample was injected into the core in an amount of 20% of the pore volume (i.e., the first injection fluid). Sample 3 was prepared using the components listed in table. 1 to form a microemulsion. This microemulsion was naked as the first injected liquid into the core under pressure in an amount of 10% of the pore volume.
    As follows from the results given in Table. I, when used
    ORPHA 1 achieves a higher oil recovery efficiency than with sample 2, and is comparable with sample 3 (i.e., with a microemulsion). Thus, since no oil is introduced into the subterranean formation, the proposed method is economical.
    Example 3. In a chemical glass, various first injected liquids were prepared by adding 6.0% YOS-Na to it with different DS contents in the effective component as surfactant, 3, OZ amyl alcohol as an auxiliary surfactant and 91% an aqueous solution of sodium chloride containing 5 sodium chloride dissolved in demineralized water as brine. The resulting mixture was stirred at 100 rpm for 10 minutes at.
    A second injection fluid was prepared by dissolving 1500 ppm xanthan gum in brine.
    The ability to form micro-emulsions, the ability of the resulting emulsions to reduce the surface
    interface tension and efficiency when extracting the oil of the first injected fluids was rated by. the same way as in example 2. The results are shown in table. 2
    Example A. Various first injected fluids were prepared in a chemical glass with 6,055 С С „YOS-Na, Co-С, YOS-Mg or Cjg-Cjj YOS-K as surfactant, 3, OZ amyl alcohol and 9IZ brine. containing a given amount of sodium chloride or a mixture of sodium chloride with calcium chloride or magnesium chloride. The obtained mixture was stirred at a speed of 100 rpm / I at.
    The second injected liquid was prepared by dissolving 1500 ppm xaitanic resin in brine.
    The ability to form micro-emulsions, the ability to reduce surface tension and the interface of the microemulsions obtained, and the degree of oil recovery using the first injected liquids were evaluated in the same way as in example 2.
    The results are shown in Table. 3
    权利要求:
    Claims (3)
    [1]
    1. A method for extracting oil from oil-bearing subterranean formations in which at least one injection and one production well has been drilled, by injecting two studs of two injected fluids through the injection well and pumping oil through the production well, and so that, in order to increase the recovery of oil, in the first stage the first injected fluid is injected into the formation, consisting of olefin sulfonate with an internal unsaturated bond, having 10-26 carbon atoms and containing 20 hours. Z or less disul phonate, auxiliary surfactant
    and brine containing 1-12 wt.X. inorganic salts, having a viscosity at 1-16 cP, in the following ratio of components, wt.%: The specified olefin sulfonate with an internal unsaturated bond 1-30 Auxiliary surfactant 0.1-20 Brine containing 1-12 wt.% inorganic salts 50-98.9, and in the second stage an aqueous, polymer solution with a higher viscosity than the viscosity of the fluid injected into the formation in the first stage is injected.
    [2]
    2. A method according to claim 1, characterized in that an olepheny sulfonate with an internal unsaturated bond is obtained by sulfonation of an olefin with an internal unsaturated bond containing, as the main component, a mono-olefin of vinylene type containing 10-26 carbon atoms and having a general formula
    R-CH-CH-R,
    where R and R are independently one of the other radicals of straight-chained or branched hydrocarbons with one or more carbon atoms with a total number of carbon atoms in the radicals of 8-24,
    followed by neutralization of the sulfonated products with the corresponding osovia, and then not necessarily
    141952712
    hydrolytic non-hp razonedannyh products, where n is the number from O to p | tmerno A;
    Comrade
    [3]
    3. The method according to p. I, characterized in that as an auxiliary surfactant injected liquid contains a substance of the general formula
    R 0 () n N,
    R is an alkyl or alkenyl group having 3 to 8 carbon atoms, when p is O, or R is an alkylene, alkenyl, phenyl or alkylphenyl group, having 6 to 15 carbon atoms, when n is 0.
    X is a comparative example;
    X is determined after appropriate dilution using a rotating droplet type strain gauge.
    Table 1
    Internal olefin sulfonate C, -CpYOS-NaCtj-Cf7YOS-Na
    The content of disulfonate, Z to the effective component
    Microemulsions
    Interfacial voltage, X 10 dyn / cm
    Oil recovery, Z
    Viscosity of the injected fluid at, cP
    Viscosity of liquid xanthan gum (1500 ppm 57 NaCl solution) at cps
    Character
    one
    ABOUT.
    With „-C„ IM-lto
    I
      0.5
     TWGTLT, W 1 (G from / cm
    "1MCH" PM fT, I places | ShZH "| 1T) W Lvostv, cV
    table 2
    17
    17
    17
    17
    t sh in t l}
    Ponait MU ((
    with "h: n to" -H | e, -c „that h c ,, - c ,, Toe-iu with„ -СцТо “- I 103
    iII4I10
    0.1
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP58057784A|JPH0331874B2|1983-04-04|1983-04-04|
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