• 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 micellar slug for use in the recovery of oil, the slug containing a hydrocarbon, an aqueous medium, a surfactant, and a cosurfactant. The surfactant contains as essential components (a) at least one alpha-olefin sulfonate having 10 to 30 carbon atoms and (b) at least one ethoxylate selected from the group consisting of polyoxyethylene alkyl ethers and polyoxyethylene alkylphenyl ethers in a weight ratio of component (a) to component (b) of 8/2 to 3/7. The micro-emulsion can be formed from this micellar slug in a wide composition range. Furthermore, this micellar slug has an excellent salinity tolerance and hard-water resistance.
    公开号:SU1473721A3
    申请号:SU833564897
    申请日:1983-03-15
    公开日:1989-04-15
    发明作者:Морита Хироси；Кавада Ясуюуки；Ямада Юниси；Юкигаи Тосиюуки
    申请人:Лион Корпорейшн (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to the oil industry, in particular to the extraction of oil using a micellar mixture capable of forming microemulsions with highly mineralized water.
    The purpose of the invention is to increase the oil-driving ability of the composition by reducing interfacial tension between the micelle mixture and oil and resistance to hard water.
    The micelle mixture for oil production consists of hydrocarbon, water, and alcohol, a surfactant, and as a surfactant
    it contains a mixture of α-α-olefin sulfonate and ethoxylate selected from the group consisting of (1) a polyoxyethylene alkyl ether of formula
    h
    WITH
     uh
    RCHCfyCHjO) -: - H,
    where R, is a linear or branched alkyl or alkenyl group containing 10-18 carbon atoms; m is the number of 1-10,
    or a group (I) of polyoxyethylene alkylphenyl ethers of formula

    s
    RЈO ° CHiCHi ° HH,
    Where bc is a linear and branched alkyl group containing 6–15 carbon atoms; p - number 1-15,
    when the mass ratio / -olefin sulfonate to ethoxylate 5.5: 1.5 3: 6 in the following ratio of components, wt.%:
    Hydrocarbon 10-70
    PAV6-14
    Alcohol0,8-6
    Water10-80
    Micellar mixtures used for oil production are transparent microemulsions. The aqueous medium used in the formation of the micelle mixture includes soft water, water containing inorganic salts, and saline solutions. For example, in the formation of a micellar mixture, rainwater, river water, lake water, subsoil water, oil reservoir water and seawater can be used.
    The micelle mixtures have excellent resistance to hard water and resistance to alkali metal salts. Water or saline solution (brine) containing about 0-10 wt.%, Preferably 0.1-8 wt.% Of inorganic salts may be used to obtain micellar mixtures. Examples of inorganic salts contained in water (or brine) are sodium chloride, KCl, sodium sulfate and potassium sulfate. For example, sea water contains about 3.5% by weight of inorganic salts containing about 1600 ppm, based on magnesium ions, divalent metal ions.

    Suitable α-olefin sulfonates, contained as one component of the surfactant mixture in micellar mixtures, are sulfonates having 10-30 carbon atoms, chosen appropriately depending on the nature of the oil fields and underground sources and on the types of water (or brine) and used surfactants. with {-0-lefin sulfonates are predominantly sulfonates containing 50 wt.% or more " (α-α-olefin sulfonates having 14-22 carbon atoms.
    to
    15
    , 737214
    N-Olefin sulfonates can be their alkali metal salts, ammonium salts and salts of organic amines. In most cases, the countercations are sodium, potassium, ammonium and alkene ammonium. Sodium salts are readily available at low cost.
    Examples of the α-olefin sulfones used in the formation of the mycelial mixtures of this invention are 1-dodecene sulfonate, 1-tetradecene sulfonate, 1-hexadecene sulfonate, o-olefin sulfonates (AOC) having 10-14 carbon atoms, AOC having 14-16 carbon atoms, AOC having 14-18 carbon atoms, AOC having 16-18 carbon atoms, and AOC having 20-24 carbon atoms.
    The ethoxylates contained as another component of the surfactant in micellar mixtures are those having the following common forts, mules
    Ro4cH2Crl20) -mH,
    I.
    five
    five

    0
    0
    five
    vg-C ° NsNgSh2obn, and
    where R ,, is alkyl or alkenyl
    a straight or branched chain group containing 10-18 carbon atoms; R2 is an alkyl group with direct
    or branched chain containing 6-15 carbon atoms;
    m 1-10 p 1-15.
    Typical examples of polyoxyethylene ethyl esters of general formula I are polyoxyethylene hexyl ether (m 1), polyoxy ethylene octyl ether (m 2), polyoxy ethylene decyl ether (m 2.5), polyoxyethylene leondedecyl ether (m 3) , polyoxyethylene tetradecyl ether (t 3.5), polyoxyethylene hexadecyl ether (t 4) and polyoxyethylene-1 tadecyl ether (t 5).
    Typical examples of polyoxyethylene alkylphenyl ethers having the general formula II are polyoxyethylenhexyphenyl ether (n), polyoxyethylene octylphenyl ether (n 2), polyoxyethylenenonylphenyl ether (4,5 and 6), polyoxyethylene decylphenyl ether polic
    5I /
    polyethylene heterldeshfenl ether (p 7), polyoxyethylene tetradesh phenyl ether (p 8), and polyoxethylenpentade phenyl phenyl ether (p 10).
    The intervals of the composition of micellar mixtures capable of forming microemulsions vary depending on the ratio of o-olefinsulfonate and ethoxylate in micelle mixtures. Microemulsions can form over a wide range of compositions. Therefore, when the medellar mixtures are injected under pressure into underground tanks, microemulsions can be kept within a wide range of composition from changing their composition caused by mixing with oil and groundwater. The weight ratio of α-olefin sulfonate to ethoxylate, which is smaller or larger than the mentioned composition interval, results in a narrow composition interval capable of forming microemulsions, and therefore is unsuitable for practical use.
    The micelle mixtures contain about 6-14% by weight of the surface-active agent, taking into account both the low tension on the interface and the reasonable cost.
    Hydrocarbons used as an oil component include, for example, petroleum, liquefied petroleum gas, crude gasoline (naphtha), kerosene, diesel oil, and fuel oil. The recovered oil is used in most cases because of its low cost and availability, and also because of its composition, similar to the composition of oil contained in underground sources. As mentioned, micelle mixtures can contain 4–90 May. % hydrocarbons. A suitable concentration of hydrocarbons is 10 to 70 wt.%, due to which an oil-in-water (M / V) emulsion is formed, since the use of a large amount of hydrocarbons is uneconomical.
    Joint surfactants used in the formation of the micellar mixtures of the present invention are an essential component for the formation of microemulsions associated with surfactants. The surfactants used are alcohols, such as alcohols having 2- to 8 hydrocarbons, ethylene glycol monoethers, having 1 -five
    15
    20
    73
    Q 25
    ,
    thirty
    35
    five
    0
    five
    7216
    carbon atom, and diethylene glycol monoethers of alcohols having 1-5 carbon atoms. Examples of such alcohols are ethanol, propanols, butanols, pentanols, hexanols, 2-ethylhexa-nanol or other octanols, methoxyethanol, ethoxyethanol, propoxyethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monobutyl methyl etheralide, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monobutyl ethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monobutyl ethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monobutyl ethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monobutyl ethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monobutyl ethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monoobethyl ethanol, butoxyethanol, diethylene glycol monomethyl ether, diethylene glycol monoobethyl ethanol, propanol, butyl alcohol
    The surfactants used may be contained in micelle mixtures in an amount of 0.1-20% by weight. However, it is advisable to use surfactants in an amount of 0.8-6% by weight in terms of the stability of the microemulsion and the ability to reduce the interfacial tension between the oil and the mixture.
    Since ethoxylate is used as one of the components of the surfactant of micellar mixtures, micellar mixtures have excellent resistance to hard water and salinity tolerance. Accordingly, when micellar mixtures are injected under pressure into underground tanks, microemulsions can be maintained in a wide range of compositions without changing their composition when mixed with oil and groundwater. In addition, the viscosity of the proposed micellar mixture can be controlled over a wide range by appropriately selecting the type of hydrophobic group and suppressing the number of moles of ethylene oxide ethoxylate and the composition ratio. Considering that microemulsions should be stored in underground tanks, the viscosity of the micellar mixtures should be slightly higher than the viscosity of oil in underground tanks.
    The use of the micelle mixture according to the invention makes it possible to achieve a high efficiency of oil production in comparison with that achieved using mixtures containing petroleum sulfonic acids, by using produced water with a high interval of salt concentration, i.e. from a low concentration at which petroleum sulfonic acids (typical surfactants for micellar displacing agents) can be used, to a high concentration at which petroleum cannot be used.
    At the same time, the viscosity of these micelle mixtures can be adjusted as desired over a wide range of 7,773,721
    le by selection of the corresponding ethoxidate. To do this, conventional thickened agents can be added to the micellar mixtures. Examples of thickened agents used in the formation of micellar mixtures are heteropolysaccharides produced by microorganisms, naphthalene sulfonic acid condensates and formaldehyde condensates, the content of liquid fuels in isacrylamides, polyacrylates, polyacrylates, polyacrylates, polyacrylates, polyacrylates, polyacrylates, polyacrylates, polyacrylates, polyacrylamide condensates, polyacrylamides, polyacrylates, polyacrylates, polyacrylates, polymers, polyacrylates, polymers, polyacrylates, polyacrylates, polymers, polyacrylates, polymers, polyacrylates, polymers, polyacrylates, polymers, polymers, polyacrylates, polyacrylates, polyacrylates
    The micelle mixtures of this invention are easily obtained using any known method. For example, hydrocarbons, a surfactant, an aqueous medium, and co-surfactants can be mixed in any order of mixing using conventional mixing devices, mixing temperatures and pressures at which the mixing is performed.
    Oil can be extracted from underground reservoirs by 25 using any conventional method of micelle development using the micellar mixtures of the invention.
    The formation of microemulsions was evaluated visually, and the interfacial tensions between micellar mixtures and oil and viscosity data were determined after the formation of these microemulsions, and the following symbols were used for visual assessment: o - microemulsion was formed; x - suspension formed or two-phase separation occurred .40
    The interfacial tension between the micellar mixtures and water were the same as the interfacial tension between the micelle mixtures and oil. These values were measured using a strainer of the instrument type with a rotating droplet at 25 C. The viscosity values were also determined at 25 ° C using a Brookfield viscometer.
    For testing, to determine the efficiency of oil production, a rod from Berea sandstone with a diameter of 3.8 and a length of 14 cm was used, the permeability of which was approximately 500 mD (millidarcy), and the porosity was approximately 20%. The rod, sufficiently saturated with brine, was placed in a mandrel.
    35
    45
    50
    55
    eight
    for the rod, and then liquid fuel was injected under this pressure with a flow rate of 6 ml / min until the brine was completely stopped. Then, under pressure with the same flow rate, the brine was injected according to the method with a water displacer until 5 0
    50
    0
    five
    five
    0
    five
    the flowing fluid did not reach a level below 0.1%, i.e. carried out the extraction of liquid fuels. After the implementation of the water expeller method, the mandrel for the rod and the microemulsions were used for the implementation of the method with the micelle propellant. Such microemulsions were first injected under pressure into the rod in an amount of 10% by volume of the total pore volume, and then under pressure a solution of xanthan resin in brine in an amount up to 100% by volume of the total pore volume and, finally, in an amount up to 100% by volume of brine volume was injected around the pore volume. Thus, the liquid fuel was extracted. The feed rate of the pressurized fluid was 2 feet / day (0.61 m / day). The oil recovery efficiency was determined by measuring the amount of water in the brine after testing according to a toluene azeotropic method in order to convert the amount of liquid fuel to be converted.
    Example 1. The micellar mixed compositions were prepared by mixing 7% by weight of a C 14-C g o-olefin sulfonate (AOC-Na C H-C 1-8) with 7% by weight of non-ionic surfactants (see Table 1) , 6% by weight of n-amyl alcohol as a co-surfactant, 40% by weight of liquid fuel (ASTM liquid fuel, sample 2) as hydrocarbon and 40% by weight of brine containing 2% sodium chloride.
    The results obtained in conjunction with the used nonionic surfactants are shown in Table. one.
    Example 2. Micellar mixed compositions were prepared by mixing in the amounts indicated in Table. 2, a mixture in the ratio of 1: 1 petroleum sodium sulfonate TRS-10 (trademark produced by Witco Chemical Corporation, USA) or AOC-Na C, in polyoxyethylene dauryl ether (t 3), isopropyl alcohol or K-amyl alcohol , liquid Table 3
     Between micelle mixtures to oil.
    Table 4
    Polyoxyethylene nonylphenyl ether (n
     5),% 2.5-1.0 2.0
    Isopropyl alcohol,% - 3,03,0
    Isobutyl alcohol,% - - 2.0 0.8 1.5
    n-Amyl alcohol,% 2.0 Kerosene,% 402020 - Liquid fuel,% 40 - 40 - 15 Brine 0.5% sodium chloride,% -50-- - - Same as 2%,% 50 -70 The same, 10%, -72.8 77.5
    Sea water,% - - 50 Visual assessment of interool tensions,
    10-3dn / cm4,59 6,675.27 1.2 8.7 7.4 Viscosity, cp38 1723 65 13 15 Oil recovery efficiency,% 88 8788 89 85 87
    Between micelle mixes and oil.
    AOC-Na С, 2,% - - - 1.4
    AOC-Na CH-C, g,% 4.02.0 1.0 3.0 3.6
    AOC-Na C4o-Cij4,% 1.22.0 1.8 3.0 Polyoxyethylene lauryl ether (),% - - - 1.5 Fulfoxyethylene nonylphenyl ether (P 5),% 2.84.0 5.2 3, 0 0.7
    Ioprrpshtovy alcohol,% - - 0.5 Isobutyl alcohol,% - - - 2.8
    n-Amyl alcohol,% 2,02,0 2,0 0,5
    Kerosene,% -35 10
    Liquid fuel,% 3045 70 Brine 0.5% sodium chloride,% 20
    The same, 2%,% 4555 The same, 5%,% 60-80
    Visual assessment of interfacial tension
    BUT-Zdn / sm0,456,32 7,89 9,73 3,2 Viscosity, sp8943 27 57 30 Oil recovery efficiency,% 8587 86 84 89
    Between micelle mixes and oil.
    Propp EPI .Z
    Table. 6
    1473721
    1Polyoxyethylene oxide ether (t - 2)
    2Polyoxyethylenelauryl ether (t 5)
    3Top (t 15) x
    4Polyoxyethylene stearyl ether (t 4)
    5The same (t 8) o
    6 Polyoxyethylene octylphenyl O (ether 2)
    7 Polyoxyethylene octyl phenyl ether (p 6)
    8 Polyoxyethylene nonylphenyl
    ether (p 5) o
    9The same (n 10) o
     (n 20) x
    11Polyoxyethylenodedecylphenyl
    ether (p 7) o
    12The same (p. 12) o
    13Pluronic
    14Pluronic R-84 x
    15Tetronic 702 x
    Ethylene oxide addition product of polypropylene glycol (40% ethylene oxide, molecular weight of polypropylene glycol 1-200), Adduct of ethylene oxide and polypropylene glycol (40% ethylene oxide, molecular weight of polypropylene glycol 2250). The product of the addition of ethylene oxide and propylene glycol (20% ethylene oxide, molecular weight of polypropylene glycol 2500). Between the micelle mixture and oil.
     Myell Mixed Mixes.
    12 Table I


    62
    34
    44
    36 71
    35
    6.88 4.72
    47 26
    7.11 9.72
    43 22
    T in l and c "2
    kim fuel used in example 1, and brine, the content of sodium chloride in which was 2%.
    The results obtained, together with the ratios between the components of the composition, are given in Table. 2
    As can be seen in their table. 2, micelle mixtures acceptable for the preparation of microemulsions allow for higher oil recovery efficiency than the use of micellar mixtures containing petroleum sulfonic acids (see examples 22 and 23, as well as 28 and 29).
    Example 3. Micellar blended compositions were prepared by mixing 14 or 12 wt.% Mixtures in various proportions of AOC-Na C (4.-C and polyoxyethylene-laural ether (T 3): 6 wt.% N-amyl alcohol or 3% by weight of isopropyl alcohol) 40% by weight of the liquid fuel used in Example 1. or 30 wt.% kerosene and 40 or 55% brine with a sodium chloride content of 2%.
    The results obtained, together with the ratios between the components of the composition, are given in Table. 3
    The results table. Figure 3 shows that the weight ratio between c (α-olefin-Sulfonate and ethoxylate) should be in the range of 5.5; 1.5-3: 6, which makes it possible to prepare micelle mixtures acceptable for the formation of microemulsions in a wide range of compositional changes.
    Example 4. Mixed micelle compositions were prepared using ct-olefinsulfonate, poloxyethylenelauryl ether and polyoxyethylene nonylphenyl ether as surfactants.
    Q 5
    0 5
    0
    0
    five
    The results obtained in conjunction with the compositions of micellar mixed compositions are given in Table. 4, 5 and 6.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    A micelle mixture for oil production, containing a hydrocarbon, a surfactant, an alcohol, and water, characterized in that, in order to increase the oil tightness of the composition by reducing the interfacial tension between the micellar mixture and oil and hard water, as a surfactant, it contains a mixture of / -olefin sulfonate containing 12-24 carbon atoms and an ethoxylate selected from the group consisting of (1) a polyoxyethylene alkyl ether of formula
    R O - (CHAHNO N,
    where R1 is a linear or branched alkyl or alkenyl group containing 10-18 carbon atoms; m 1 ... 10,
    or from group (ii) a poly-ethylene alkylphenyl ether of formula
    R2 O 0 CH2CH2 ° h; H
    where R.J is linear or branched
    an alkyl group containing 6 to 15 carbon atoms; n 1 ... 15,
    at a mass ratio of o-olefinic sulfonate and ethoxylate of 5.5: 1.5-3: 6 in the following ratio of components in the mixture, wt.%:
    Hydrocarbon 10-70
    PAV6-14
    Alcohol0.8-6.0
    Water10-80
    61 Polyoxyethylene decyl ether (t 1)
    62Polyoxyethylene stearyl ether (t 10)
    63Polyoxyethylenehexyl nyl ether (p 1)
    64 Polyoxyethylene leondecyl phenyl ether (15)
    65 Poly (ethylene pentadecylphenyl ether)
     12)
    66 The same (p 15) 67 The same (p 18)
     Comparison
    Table 7
    74 31 91 22 37
    25
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1419527A3|1988-08-23|Method of extracting petroleum from oil-bearing underground beds
    US4597879A|1986-07-01|Micellar slug for oil recovery
    US4733728A|1988-03-29|Micellar slug for oil recovery
    US4537253A|1985-08-27|Micellar slug for oil recovery
    Yang et al.2010|Low-cost, high-performance chemicals for enhanced oil recovery
    US4555351A|1985-11-26|Micellar slug for oil recovery
    US4110229A|1978-08-29|Salinity tolerant surfactant oil recovery process
    US4549607A|1985-10-29|Micellar slug for oil recovery
    US4017405A|1977-04-12|Soluble oil composition
    SU1473721A3|1989-04-15|Micellar mixture for oil production
    US4013569A|1977-03-22|Aqueous anionic surfactant systems containing aromatic ether polysulfonates
    US3920073A|1975-11-18|Miscible flooding process
    US4269271A|1981-05-26|Emulsion oil recovery process usable in high temperature, high salinity formations
    US4434062A|1984-02-28|Oil displacement enhanced by lyotropic liquid crystals in highly saline media
    CA1221621A|1987-05-12|Staged preformed-surfactant-optimized aqueousalkaline flood
    US3356138A|1967-12-05|Oil recovery process utilizing liquefied petroleum gases and heavier hydrocarbons
    Puerto et al.2018|Laboratory studies of ternary surfactant formulation for EOR in oil-wet, high-temperature carbonate formations
    GB2138866A|1984-10-31|Micellar slug for oil recovery
    US4528105A|1985-07-09|Micelle solution compositions for recovering crude oil
    US4460481A|1984-07-17|Surfactant waterflooding enhanced oil recovery process
    US3714062A|1973-01-30|Straight chain sulfonates for use in solubilized oil-water solutions for miscible waterflooding
    GB2135713A|1984-09-05|Micellar slug for oil recovery
    EP2536808A1|2012-12-26|Surfactant systems for enhanced oil recovery
    US3698479A|1972-10-17|Solubilized oil-water solutions suitable for miscible flooding
    GB2174438A|1986-11-05|Micellar slug for oil recovery
    同族专利:
    公开号 | 公开日
    US4534411A|1985-08-13|
    JPS58160491A|1983-09-22|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2668429C2|2013-05-31|2018-10-01|ДАУ ГЛОБАЛ ТЕКНОЛОДЖИЗ ЭлЭлСи|Low temperature stabilized foam-forming composition for enhanced oil recovery|US3506070A|1967-12-26|1970-04-14|Marathon Oil Co|Use of water-external micellar dispersions in oil recovery|
    US3508611A|1968-07-22|1970-04-28|Marathon Oil Co|Molecular weight of hydrocarbon influencing the thermostability of a micellar dispersion|
    US3536136A|1969-09-25|1970-10-27|Marathon Oil Co|Oil recovery process with cosurfactant influencing the thermostability of micellar dispersions|
    US3990515A|1974-12-24|1976-11-09|Sun Oil Co|Waterflooding process with recovery of lost surfactant|
    CA1031686A|1974-12-24|1978-05-23|Sun Oil Company |Secondary recovery process and surfactant compositions useful therein|
    US3981361A|1975-07-31|1976-09-21|Exxon Production Research Company|Oil recovery method using microemulsions|FR2548676B1|1983-07-04|1986-03-21|Rhone Poulenc Spec Chim|BIOPOLYMER COMPOSITIONS AND THEIR PREPARATION PROCESS|
    US4736795A|1987-03-24|1988-04-12|Atlantic Richfield Company|Composition and process for enhanced oil recovery|
    US5110487A|1989-04-03|1992-05-05|Chevron Corporation|Enhanced oil recovery method using surfactant compositions for improved oil mobility|
    US5095989A|1991-02-21|1992-03-17|Texaco Inc.|Microemulsion method for improving the injectivity of a well|
    GB2259518B|1991-09-05|1996-02-14|Shell Int Research|Micro-emulsion cleaner composition suitable for use in seawater|
    US5942468A|1998-05-11|1999-08-24|Texas United Chemical Company, Llc|Invert emulsion well drilling and servicing fluids|
    DE102005026716A1|2005-06-09|2006-12-28|Basf Ag|Surfactant mixtures for tertiary mineral oil production|
    CN102803433A|2009-05-05|2012-11-28|斯特潘公司|Sulfonated internal olefin surfactant for enhanced oil recovery|
    CN103045221B|2011-10-17|2015-01-21|中国石油天然气股份有限公司|Surfactant flooding system and application thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP57040290A|JPS58160491A|1982-03-16|1982-03-16|Micelle solution for recovery of petroleum|
    [返回顶部]