• 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 increasing the yield of crude oil reservoirs exploited by subterranean burning or by steam flooding. The process of the present invention is carried out by introducing an aqueous salt solution into the oil reservoir, then producing salt-crystals in the pores of the oil-bearing rock formation by total or partial elimination of the solvent, or by decreasing the solubility of the salt, and optionally resolving the salt-crystals separated out partially or totally by pressing in additional solvent, and optionally forming salt-crystals in an other part of the reservoir.
    公开号:SU1590050A3
    申请号:SU864027849
    申请日:1986-07-19
    公开日:1990-08-30
    发明作者:Медьери Михай；Конц Иштван；Паал Тибор；Тисаи Дьердь；Ситтар Антал
    申请人:Мадьяр Сенхидрогенипари Кутато-Фейлесте, Интезет (Инопредприятие)；Кеолай Еш Фельдгазбаньасати Валлалат (Инопредприятие)；
    IPC主号:
    专利说明:

    The invention relates to a method for increasing production from fields developed by gas, underground combustion, or steam.
    The purpose of the invention is to increase the efficiency of the method.
    When gas is displaced, none of the known methods leads to a satisfactory result. In addition, they require the use of expensive foaming surfactants, polymers, dispersing agents, which makes these events uneconomical. The application of the known methods is also hampered by the fact that the interaction of the oil-bearing rock and the fluid in the reservoir can change the composition of the compounds, which makes the displacement process uncontrollable.
    The proposed method is carried out by introducing into the field an aqueous solution of salt and the subsequent formation of salt crystals in the pores of the oil-bearing rock due to complete or partial removal of the solvent.
    i For an aqueous solution, use one. well, or more inorganic salts, for example sodium hporide, potassium chloride, sodium sulfate, etc., or a double salt, for example, mixed potassium sulfate and aluminum. Salt may also be formed in situ in the field. Particularly preferably used
    SP
    se
    sd

    s
    15900504
    volume change 1,225; the density of oil in the rock at 20 ° C is 819 the initial relative water content is 0.3.
    Primary production from the rock is carried out by reducing the pressure to 36 atm. The yield (extraction) (E) due to the displacement due to the action of dissolved gas and water is equal to 0.38.
    After the primary mining, the field is then developed by a secondary extraction method using natural gas containing 80% sodium dichloride as a salt for an aqueous solution.
    Salt crystals in the oil-bearing rock are formed due to partial or complete removal of the solvent using known methods, for example, by shrinking, decomposing, etc.
    The solvent is removed with a water removal agent.
    Highly permeable portions of heterogeneous oil-bearing rock have an undesirable effect on volume displacement and on crystals hindered by crystals or blocked by carbon monoxide.
    Two adjacent areas of oil field with identical pa10
    currents
     If desired, the precipitated salt crystals are partially or completely dissolved by injecting additional solvent into the deposit, with the atom being possible, the salt crystals can be re-formed in other zones of the deposit. In this way, depending on the presence of: xc conditions, it is possible to control the permeability of different sections of: 25h-bearing rocks.
    The increase in production from oil-bearing rocks, developed by the introduction of gas, underground burning or steam injection, is achieved by introducing water-Q salt solution into the field and the formation of crystal salt in the pores of the oil-bearing rock due to complete or partial removal of the solvent
    or removal of ai eHTOM. It is possible to re-dissolve (partial or complete) of the separated salt crystals by pumping an additional solution of mineral oil into the field, with the possible formation of salt crystals in other parts of the deposit; The water removal agent is ethanol and / or methanol.
    The displacement of oil saline, d carbon,. introduced into the oil-bearing rock, has a positive effect on the distribution of gases between the water and the oil phase, especially on the distribution of gases that are well soluble in water, such as carbon dioxide.
    Example 1. Porous sandstone has the following parameters: porosity 0.21 (limit values 0, and 0.23) permeability 0.060 jUM (limit values 0.01-0.1 hm): temperature
    The dimensions and watering developed from five points are used to compare the known method using carbon dioxide and the proposed method.
    Each of the sites with five points of watering has a volume of ENT of 17,500 m and contains initially 10,000 m of oil. In primary production, 3800 m of oil is extracted (Е R, 0.38).
    Production from the first site in the usual way using carbon dioxide is carried out as follows.
    The pressure in the layer of oil-bearing rock is increased to 100 atm by the introduction of natural gas containing carbon dioxide through the pumping well, and controlled production of oil is produced through the production well. When natural gas containing carbon dioxide is injected in an amount of 0.36 pore volume (at 100 atm and 64 C), oil is additionally obtained in an amount of 0.03, and then water-gas is introduced at 100 atm (natural gas containing 80% dioxide and water is fresh).
    50
    55
    layer initial pressure; in the atmosphere of 100 atm; dissolved gas to oil ratio 56 coefficient
    As a result of gas injection in an amount of 0.2 pore volume, the oil yield is increased by another 0.12. At the end of the secondary dobiye, water is pumped in an amount of 0.3 of the pore volume again and an additional oil yield of 0.03 is obtained. The result is the output of secondary oil production (ER, J), equal to 0.18, i.e. The total oil yield obtained (E, is equal to 0.56. To the first section, developed by the usual method of secondary extraction using carbon dioxide, can be applied0 5
    Q
    0
    The carbon, dimensions and watering developed from five points are used to compare the known method using carbon dioxide and the proposed method.
    Each of the sites with five points of watering has a volume of ENT of 17,500 m and contains initially 10,000 m of oil. In primary production, 3800 m of oil is extracted (Е R, 0.38).
    Production from the first site in the usual way using carbon dioxide is carried out as follows.
    The pressure in the layer of oil-bearing rock is increased to 100 atm by the introduction of natural gas containing carbon dioxide through the pumping well, and controlled production of oil is produced through the production well. When natural gas containing carbon dioxide is injected in an amount of 0.36 pore volume (at 100 atm and 64 C), oil is additionally obtained in an amount of 0.03, and then water-gas is introduced at 100 atm (natural gas containing 80% dioxide and water is fresh).
    carbon,
    As a result of gas injection in an amount of 0.2 pore volume, the oil yield is increased by another 0.12. At the end of the secondary dobiye, water is pumped in an amount of 0.3 of the pore volume again and an additional oil yield of 0.03 is obtained. The result is the output of secondary oil production (ER, J), equal to 0.18, i.e. the total oil yield obtained (E is equal to 0.56.) The proposed method as a tertiary production method can be applied to the first section developed by the conventional secondary recovery method using carbon dioxide.
    The characteristics of the passing stream suggest that 70% of the effective layer thickness is involved in the operation.
    In the first stage of the process, 0.3 of the pore volume of the natural gas containing carbon dioxide and 0.3 of the pore volume of the concentrated sodium chloride solution are injected into the reservoir, and then 0.05 of the ethanol pore volume, additionally 0.3 of the pore volume of dried carbon dioxide and 0.5 of the pore volume of water,
    For tertiary production using the proposed method, an additional 20% of oil is obtained (E (s f 0.2)), i.e. the resulting oil yield (Enj) is 0.76.
    Example 2. The proposed method produces secondary production of oil from the second section.
    0.3 pore volume with doses of approximately 0.05 pore volume and less, and at the end a gas of 0.15 pore volume is introduced into the layer. The increase in oil recovery is 24%.
    In the last stage of the process, fresh water is pumped in an amount of 0.3 of the pore volume and an increase in the oil yield is obtained by 12%.
    As a result of secondary extraction no-j, an additional amount of oil (E, 0.39) is obtained, and the total oil yield rises to Ep2 0.77. This result exceeds the oil yield obtained using the conventional secondary production method by 0.21.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    The method of extracting oil from vertically lying heterogeneous oil fields by pumping gas and water salt solutions and forming
    The first stage of the method, i.e. above- .25 ste the zone of salt crystals precipitated from
    Pressurizing the p layer to 100 atm with natural gas containing 80% carbon dioxide at a controlled oil output, identical to the first stage of additional oil recovery, is carried out completely or partially from the first section.
    solution, and the movement of this zone in the reservoir, characterized in that, in order to increase the efficiency of the method, the formation of a zone of crystals
     When pumping gas in an amount of 0.36 pore volume, an additional amount of 0.03 oil is obtained. Then, in me; - stoladenie pumped in a concentrated salt solution in an amount of 0.3 pore volume and carbon dioxide containing natural gas in the amount of
    the salts are carried out by completely or partially removing the solvent from the aqueous
    solution, and the movement of this zone in the reservoir, characterized in that, in order to increase the efficiency of the method, the formation of a zone of crystals
    a saline solution at a paste temperature by injection or a water-removing agent; moreover, a concentrated solution of sodium chloride is pumped into the reservoir as aqueous salt solutions, and ethanol and / or methanol is added to the quality of the water agent.
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    同族专利:
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    AT391347B|1990-09-25|
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    引用文献:
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    US3104714A|1963-09-24|Apparatus to prevent fouling of wire |
    US2903065A|1957-08-07|1959-09-08|Pure Oil Co|Secondary recovery of oil from reservoirs by successive precipitation|
    US3072185A|1958-03-17|1963-01-08|Pure Oil Co|Improved flooding method for the recovery of petroleum|
    US3055423A|1959-05-04|1962-09-25|Phillips Petroleum Co|Controlling selective plugging of carbonaceous strata for controlled production of thermal drive|
    US3070167A|1959-07-30|1962-12-25|Jersey Prod Res Co|Device for pumping tools into wells|
    US3180414A|1961-03-27|1965-04-27|Phillips Petroleum Co|Production of hydrocarbons by fracturing and fluid drive|
    US3331438A|1964-09-30|1967-07-18|Mobil Oil Corp|Method for in situ retorting of oil shale employing artificial barriers|
    US3292702A|1966-06-07|1966-12-20|Exxon Production Research Co|Thermal well stimulation method|
    US3530935A|1968-06-03|1970-09-29|Brown Oil Tools|Motor for running and retrieving well tools|
    US3543852A|1968-12-16|1970-12-01|Otis Eng Corp|Well tools|
    US3566967A|1969-06-19|1971-03-02|Pan American Petroleum Corp|Thermal plugging with silicate solutions|
    US4026357A|1974-06-26|1977-05-31|Texaco Exploration Canada Ltd.|In situ gasification of solid hydrocarbon materials in a subterranean formation|
    US4293283A|1977-06-06|1981-10-06|Roeder George K|Jet with variable throat areas using a deflector|
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    US4441861A|1981-07-10|1984-04-10|Canalizo Carlos R|Well production apparatus and method|
    US4398602A|1981-08-11|1983-08-16|Mobil Oil Corporation|Gravity assisted solvent flooding process|
    SU1030534A1|1981-12-16|1983-07-23|Красноярский Отдел Бурения И Испытания Скважин Восточно-Сибирского Научно-Исследовательского Института Геологии,Геофизики И Минерального Сырья|Method for isolating low-permeable bed of well|
    US4418751A|1982-03-31|1983-12-06|Atlantic Richfield Company|In-situ combustion process|
    US4495994A|1983-02-02|1985-01-29|Texaco Inc.|Thermal injection and in situ combustion process for heavy oils|
    US4605069A|1984-10-09|1986-08-12|Conoco Inc.|Method for producing heavy, viscous crude oil|
    US4597442A|1985-02-26|1986-07-01|Shell Oil Company|Reservoir preflushing process for increasing the rate of surfactant transport in displacing oil with injected steam and steam-foaming surfactant|US7809538B2|2006-01-13|2010-10-05|Halliburton Energy Services, Inc.|Real time monitoring and control of thermal recovery operations for heavy oil reservoirs|
    US7770643B2|2006-10-10|2010-08-10|Halliburton Energy Services, Inc.|Hydrocarbon recovery using fluids|
    US7832482B2|2006-10-10|2010-11-16|Halliburton Energy Services, Inc.|Producing resources using steam injection|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    HU844315A|HU197065B|1984-11-21|1984-11-21|Method for increasing the recovery of vertically heterogeneous petroleum reservoirs working by gas drive|
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