CN108219763A - A kind of acidizing sandstone oil reservoir slow type MH acid system and its construction technology - Google Patents

A kind of acidizing sandstone oil reservoir slow type MH acid system and its construction technology Download PDF

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CN108219763A
CN108219763A CN201810055584.0A CN201810055584A CN108219763A CN 108219763 A CN108219763 A CN 108219763A CN 201810055584 A CN201810055584 A CN 201810055584A CN 108219763 A CN108219763 A CN 108219763A
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acid
oil reservoir
sandstone oil
acidizing
slow type
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刘音
张世林
燕晓民
马田力
张伟辉
刘位
吴兆亮
李楠
杨东海
李欣
姜有才
王瑞泓
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CNPC Bohai Drilling Engineering Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/52Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
    • C09K8/528Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning inorganic depositions, e.g. sulfates or carbonates
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK 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
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/12Swell inhibition, i.e. using additives to drilling or well treatment fluids for inhibiting clay or shale swelling or disintegrating

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mining & Mineral Resources (AREA)
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  • Fluid Mechanics (AREA)
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  • Geochemistry & Mineralogy (AREA)
  • Environmental & Geological Engineering (AREA)
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Abstract

The invention discloses the water of 45~55% organic phospho acid, 5~10% sulfamic acid, 5~10% hydrogen fluoride amine, 2~4% high-temperature corrosion inhibitor, 1~3% citric acid, 10~18% formaldehyde, 0.5~1% clay stabilizer and surplus that a kind of acidizing sandstone oil reservoir includes being calculated in mass percent with slow type MH acid system;Corresponding acidizing treatment then adds in part sulfamic acid, organic phospho acid, high-temperature corrosion inhibitor, citric acid, formaldehyde and clay stabilizer using first mixing, then certain interval of time remix add in remaining sulfamic acid and ammonium acid fluoride method is added portionwise;The acidizing sandstone oil reservoir injures sandstone oil reservoir skeleton with slow type MH acid system small, it is good to be acidified plugging removal effect, it is compared to the mud acid that tradition uses, its drill core permeability rate increase multiple ratio is 3~4 times, in-place permeability is effectively increased, realizes and acidification transformation is carried out to complex lithology sandstone oil reservoir deep.

Description

A kind of acidizing sandstone oil reservoir slow type MH acid system and its construction technology
Technical field
The present invention relates to oil gas field stimulation technology field, more particularly to a kind of acidizing sandstone oil reservoir more hydrogen of slow type Acid system and its construction technology.
Background technology
Sandstone reservoir grease well acidizing mainly by injecting the acid fluid systems such as HF acid, HCl acid and HFB acid to stratum, makes Acid solution with many silicoides include quartz and clay reaction, release near wellbore zone tamper (such as iron oxide, ferrous sulfide, Clay etc.) renwing stratum permeability;The part rock of nearly well band is also can dissolve, the throat of expandable pores structure improves stratum and oozes Saturating rate.But it improves permeability and depends on many factors, if acid type selection or acid treatment process are improper, cannot not only increase production, even The chemical precipitation and other reasons that can be also generated in acidization cause oil and gas reservoir pore plugging and the underproduction.
However, the conventional acidulation liquid system including regular mud acid, hydrochloric acid etc. is applied to show during sandstone acidizing Go out following deficiency:1) reaction speed is fast, and acid just occurs immediately upon reaction when being contacted with rock or clay, causes penetration range short, acid Liquid is difficult to enter into complex lithology deep and is transformed;2) secondary precipitation, the chlorite contained in mineral and mixing are easily formed Clay is by after mud acid corrosion, it will generates a large amount of iron colloidal precipitation, the iron hydroxide of precipitation can block hole, easily cause stratum Permeability is low;And zeolite and feldspar in reservoir etc., although can be generated dissolution pore after sour corrosion, acid solution can excessively cause rock The disintegration of skeleton particle blocks hole and oil reservoir is damaged;3) high volatility, not environmentally, hydrochloric acid and mud acid both acid are easily Volatilization, especially when Hainan is when torrid areas operation, performance it is particularly evident, high volatility not only be pungent and to human body and environment It endangers larger, belongs to the acids chemicals of public security department's control.
Therefore, in order to efficiently solve the above problem, the effect of complicated sandstone oil reservoir deep transformation is improved, should be studied A kind of acid fluid system for being adapted to sandstone oil reservoir transformation of environment-friendly type, in-place permeability is improved after being transformed.
Invention content
The object of the present invention is to provide one kind to overcome drawbacks described above, realizes and complex lithology sandstone oil reservoir deep is acidified The slow type MH acid system of the acidizing sandstone oil reservoir of transformation.
It is realized it is a further object of the present invention to provide a kind of using the slow type MH acid system of above-mentioned acidizing sandstone oil reservoir The corresponding construction technology of acidification transformation is carried out to complex lithology sandstone oil reservoir deep.
For this purpose, technical solution of the present invention is as follows:
A kind of slow type MH acid system of acidizing sandstone oil reservoir, including be calculated in mass percent 45~55% it is organic Phosphonic acids, 5~10% sulfamic acid, 5~10% hydrogen fluoride amine, 2~4% high-temperature corrosion inhibitor, 1~3% citric acid, 10 The water of~18% formaldehyde, 0.5~1% clay stabilizer and surplus;Wherein, the organic phospho acid is aminotrimethylene phosphine Sour (ATMP), hydroxy ethylene diphosphonic acid (HEDP), ethylenediamine tetramethylene phosphonic acid (EDTMP) or diethylenetriamine pentamethylene Phosphonic acids (DETPMP).
Wherein, organic phospho acid plays the role of two in the system, and one prevents calcium ion from forming carbon to provide hydrogen ion Second sour calcium is to play corrosion inhibition;In addition, ensure its chemical stabilization containing a large amount of C-P keys in the molecule of organic phospho acid Property is good, and facile hydrolysis, high temperature resistant can not keep stable property in sandstone.The structural formula of sulfamic acid is:NH2SO3H, Aqueous solution has the highly acid equal with hydrochloric acid, sulfuric acid etc., has the characteristics of not volatile, odorless, minimum to human toxicity. The structural formula of hydrogen fluoride amine is:NH4HF2, it is used for identical with organic phospho acid, in the early stage for providing hydrogen ion, plays acidification sand Rock prevents calcium ion from forming the effect of calcium carbonate.Citric acid is used as ferrous stability in the system.Formaldehyde then primarily serves Sterilization and corrosion-resistant effect.Clay stabilizer is then used to after entering stratum adsorb in surface of clay, prevents water sensitivity mineral aquation Expansion and dispersion are migrated and the injury caused by oil-gas Layer
It is preferred that the high-temperature corrosion inhibitor is the condensation product of acetophenone-metaformaldehyde-cyclohexylamine, nonylphenol polyoxyethylene ether, The mixture of methanol and propilolic alcohol, four weight ratios are 10:2:6:1.
It is preferred that the clay stabilizer is organic ammonium salt and the mixture of ammonium chloride, the two weight ratio is 3:7;Wherein, have Machine ammonium salt is 1 by molar ratio:2.5~3 ethylenediamine is generated with acetic acid reaction.
A kind of construction technology of the slow type MH acid system of acidizing sandstone oil reservoir, wherein, acidizing sandstone oil reservoir is with slowly The formula of type MH acid system is as described above;Accordingly, which is walked with slow type MH acid system Specific construction It is rapid as follows:The sulfamic acid of suitable aqueous solvent and half quality is added in agitator tank first, is continued after stirring evenly to stirring It mixes and organic phospho acid, high-temperature corrosion inhibitor, citric acid, formaldehyde and clay stabilizer is added in tank, continue stirring to after mixing, incite somebody to action Gained mixed solution is delivered to underground by casing;After 2~8h is spaced, hydrogen fluoride amine, remaining half are added in into agitator tank The sulfamic acid of quality and suitable aqueous solvent, underground is delivered to after stirring evenly by mixed solution by casing.
In the construction technology, acidizing sandstone oil reservoir with the component that slow type MH acid system includes is divided into and is sent into twice Underground makes acid solution real its role is to which the acid solution into lithology sandstone is enable to keep hydrionic presence under longer time Penetration range of the border in lithology sandstone layer increases, that is, achievees the purpose that deep acidizing is transformed.
Wherein, be delivered in the blending ingredients of underground at first, sulfamic acid and part organic phospho acid first provide hydrogen from Calcium carbonate and quartz components in son dissolving rock, penetrate rock stratum and form crack;Since iron-bearing mineral content is high in stratum, pass through The effect iron-bearing mineral of acid solution will dissociate Fe3+Ion will generate Fe (OH) when residual sour pH value rises to 23Secondary precipitation, shape Into secondary injury, acidizing effect is influenced, therefore complexing of the stabilizer realization to iron ion is used as by the citric acid of addition;Inhibition Agent avoids Fe for preventing corrosion of the acid solution to pipeline and equipment3+Into formation influence acidizing effect;Clay stabilizer is then used for It adsorbs in surface of clay, prevents water sensitivity mineral hydration swelling and dispersion migration and injured caused by oil-gas Layer.
Continue to convey second batch blending ingredients after 2~8h of interval, be sent into the sulfamic acid of the other half quality on stratum to rock While hydrogen ion in rock layers is supplemented, villiaumite (i.e. hydrogen fluoride amine) reacts generation hydrofluoric acid with remaining organic phospho acid, Sandstone skeleton structure and clay mineral are dissolved, increases reservoir permeability.
Specifically, organic phospho acid, i.e. aminotrimethylenephosphonic acid (ATMP), hydroxy ethylene diphosphonic acid (HEDP), second Diamines tetramethylene phosphonic acid (EDTMP) and diethylenetriamine penta (DETPMP) are MH acid, can be occurred Step-ionization reacts, and Step-ionization goes out hydrogen ion, since organic phospho acid reacts generation hydrofluoric acid with villiaumite (i.e. hydrogen fluoride amine) Process can promote the progress of ionization reaction simultaneously, therefore after organic phospho acid encounters hydrogen fluoride amine, Step-ionization goes out hydrogen ion, And generation hydrofluoric acid HF is reacted with villiaumite, HF and the sandstone reservoir of generation react, gradually penetrate sandstone deep formation, penetrate It is good to complete acidification reservoir reconstruction effect for distance.
It is illustrated by taking diethylenetriamine penta as an example, Step-ionization process is shown below:
H5R——→H++H4R- pK1=1.0
H4R-——→H++H3R2- pK2=2.5
H3R2-——→H++H2R3- pK3=7.0
H2R3-——→H++H R4- pK4=11.4
H R4-——→H++R5- pK5> 12.0
It is not difficult to find out from above formula, since diethylenetriamine penta is pentabasic acid, including five steps electricity From process, wherein according to the dissociation constant provided, it is main ionization process that first three step, which is ionization, due to adding for later stage hydrogen fluoride amine Enter, be promoted above-mentioned ionization process, ionize out more hydrogen ions;Therefore, because the ionization process of MH acid is substep It carries out, and the presence of sulfamic acid simultaneously suitably inhibits the ionization rate of MH acid early period, avoids ionization rate mistake Soon, it realizes that hydrionic remaining time extends, is conducive to the extension of its penetration range in lithology sandstone layer, it is final to obtain deeply The effect of degree transformation sandstone layer.
Moreover, it is also resided in the advantages of MH acid can adsorb on a rock surface;In addition to physisorption with Outside, when MH acid is reacted with clay, at " thin layer " of surface of clay generation aluminium silicon phosphonate, belong to film forming effect, prevent viscous Soil and acid liquid reaction reduce the solubility of clay, so as to reduce corrosiveness of the acid solution to reservoir skeleton;Meanwhile to rock The later Ca of corrosion2+、Al3+、Fe2+、Fe3+With very strong complexing power, prevent these ions and fluorine ion, fluosilicic acid root from Son forms villiaumite precipitation, fluosilicate precipitates and blocks duct, and chelating effect can occurs in it under very low concentrations in addition, make These ions remain solution state, that is, " threshold effect " occur;Due to inhibiting and precipitation seed is prevented to generate, improve Permeability and acidification effect.
In conclusion the acidizing sandstone oil reservoir injures sandstone oil reservoir skeleton with slow type MH acid system small, acidification solution Stifled effect is good, is compared to the mud acid that tradition uses, drill core permeability rate increase multiple ratio is 2~4 times, effectively increases stratum Permeability is realized and carries out acidification transformation to complex lithology sandstone oil reservoir deep;And the system is in protection rock matrix and inhibition While clay swelling, the pollution of near wellbore zone is released.In addition, the acidizing sandstone oil reservoir is formed with slow type MH acid system Each component easily obtains, at low cost, and construction technology is simple, has good popularizing application prospect.
Specific embodiment
With reference to specific embodiment, the present invention is described further, but following embodiments absolutely not to the present invention have appoint What is limited.
Embodiment 1
The slow type MH acid system of a kind of acidizing sandstone oil reservoir, including 50 parts of DETPMP, 8 parts of amino in parts by weight Sulfonic acid, 5 parts of hydrogen fluoride amine, 3 parts of high-temperature corrosion inhibitors, 1 part of citric acid, 17 parts of formaldehyde, 1 part of clay stabilizer and 15 parts of water.
Embodiment 2
The slow type MH acid system of a kind of acidizing sandstone oil reservoir, including 48 parts of ATMP, 9 parts of amino sulphurs in parts by weight Acid, 6 parts of hydrogen fluoride amine, 3.5 parts of high-temperature corrosion inhibitors, 2 parts of citric acids, 15 parts of formaldehyde, 0.5 part of clay stabilizer and 16 parts of water.
Embodiment 3
The slow type MH acid system of a kind of acidizing sandstone oil reservoir, including 45 parts of ATMP, 10 parts of amino in parts by weight Sulfonic acid, 8.5 parts of hydrogen fluoride amine, 4 parts of high-temperature corrosion inhibitors, 2 parts of citric acids, 13 parts of formaldehyde, 0.5 part of clay stabilizer and 17 parts of water.
Embodiment 4
The slow type MH acid system of a kind of acidizing sandstone oil reservoir, including 52 parts of DETPMP, 7 parts of amino in parts by weight Sulfonic acid, 5.5 parts of hydrogen fluoride amine, 2.5 parts of high-temperature corrosion inhibitors, 1 part of citric acid, 18 parts of formaldehyde, 1 part of clay stabilizer and 13 parts of water.
Embodiment 5
The slow type MH acid system of a kind of acidizing sandstone oil reservoir, including 55 parts of EDTMP, 5 parts of amino in parts by weight Sulfonic acid, 7.5 parts of hydrogen fluoride amine, 2 parts of high-temperature corrosion inhibitors, 3 parts of citric acids, 10 parts of formaldehyde, 0.5 part of clay stabilizer and 17 parts of water.
In above-described embodiment 1~5, in addition to high-temperature corrosion inhibitor and clay stabilizer, other components are bought from commercial product. Wherein, the preparation method of high-temperature corrosion inhibitor is:It is 1 first by molar ratio:1:0.8 acetophenone, metaformaldehyde and cyclohexylamine three It kind of monomer and accounts for the hydrochloric acid (37.5wt.%) of monomer gross mass 3.5% and adds in reaction kettle and be warming up to 95 DEG C of reaction 8h, obtain The condensation product of acetophenone-metaformaldehyde-cyclohexylamine;Then it is 10 by weight ratio:2:6:1 acetophenone-metaformaldehyde-cyclohexylamine Condensation product, nonylphenol polyoxyethylene ether, methanol and propilolic alcohol mixed to get to high-temperature corrosion inhibitor.Clay stabilizer Preparation method is:It is first 1 in molar ratio by ethylenediamine and acetic acid:2.5~3 reaction generation organic ammonium salts, then with weight ratio It is 3:7 are mixed with ammonium chloride, and gained mixture can be used as clay stabilizer use.
Acidizing treatment simulation further is carried out with slow type MH acid system to the acidizing sandstone oil reservoir of Examples 1 to 5, with Its corresponding acidizing effect is evaluated.
Mimicry acidifying is tested:The core simulation sandstone that 6 pieces of ingredients are identical is taken, and is respectively put into 6 large beakers, to 6 The mix acid liquor by evenly mixing that Examples 1 to 5 provides is separately added into beaker, injects mud acid solution in the 6th beaker (12wt.%HCl+3wt.%HF) as a comparison case.The acid solution injected in each beaker there was not core completely.Core is impregnated It takes out, dries after 48h in acid solution, impregnate forward and backward weight by weighing, calculate Examples 1 to 5 and come relative to comparative example Say acid solution to the acidification of rock core as a result, i.e. core permeability increase multiple, specific formula for calculation are:A=(m1-m2)/(m1’- m2'), wherein, a increases multiple, m for core permeability1For the core initial quality of Examples 1 to 5, m2For Examples 1 to 5 Quality of the core after immersion, m1' be comparative example core initial quality, m2' it is matter of the core of comparative example after immersion Amount.
In addition, also to the acidizing sandstone oil reservoir of Examples 1 to 5 with slow type MH acid system under normal pressure to J55 steel discs Corrosion rate tested, test the corrosion mitigating effect of the system.
Test result is as follows shown in table 1.
Table 1:
As can be seen from the above table, the mud acid body which is used with slow type MH acid system relative to tradition The core permeability of system can effectively increase at least 3 times or more, to the corrosion rate > 0.708g/m of J55 steel discs2.h, there is acid The advantages of quick property formation damage is small, and acidification plugging removal effect is good, corrosion mitigating effect is good;Simultaneously as acid solution used in the system exists Not volatile during use, each additive is nontoxic or less toxic, small to human body and environmental injury.In actual use, it is sour Compatibility is good between each additive of liquid and between water flooding.
The one embodiment applied below for the practical acidification of the slow type MH acid system of the acidizing sandstone oil reservoir.
Embodiment 6
Flower xx well locations are in Hainan Fushan oil field, and small fault block is more, lithology is complex, and reservoir permeability is low, reservoir and non-storage Layer is interlaced, and interlayer relation is complicated, and reservoir sensitivity is strong.It is quick that the acid-sensitive evaluation result of the block belongs to strong acid, and Lin Jing is conventional Soil acid acidizing reaches expected effect of increasing production unobvious after acidification.Therefore, it determines to carry out acid to the well using multi-hydrogen acid system Neutralizing is stifled.Wherein, acidification liquid system includes 50 parts by weight organic phospho acids, 10 parts by weight sulfamic acids, 5 parts by weight ammonium acid fluorides, 1 Parts by weight clay stabilizer, 3 parts by weight of lemon acid, 2 parts by weight high-temperature corrosion inhibitors, 13 parts by weight of formaldehyde and 16 parts by weight are originally Water;Displacement fluid is done with+2% clay stabilizer of clear water.
Construction results compare:Well day oil-producing 3.06t/d before acidification, well day oil-producing 15.34t/d after acidification, volume increase 5 Times, it is seen that using the acidizing sandstone oil reservoir with slow type MH acid system carry out acidification de-plugging achieve highly significant volume increase imitate Fruit.

Claims (4)

1. a kind of slow type MH acid system of acidizing sandstone oil reservoir, which is characterized in that including be calculated in mass percent 45~ 55% organic phospho acid, 5~10% sulfamic acid, 5~10% hydrogen fluoride amine, 2~4% high-temperature corrosion inhibitor, 1~3% Citric acid, 10~18% formaldehyde, 0.5~1% clay stabilizer and surplus water;Wherein, the organic phospho acid is ammonia Base trimethylene phosphonic, hydroxy ethylene diphosphonic acid, ethylenediamine tetramethylene phosphonic acid or diethylenetriamine penta.
2. the slow type MH acid system of acidizing sandstone oil reservoir according to claim 1, which is characterized in that the high temperature delays Mixture of the erosion agent for the condensation product of acetophenone-metaformaldehyde-cyclohexylamine, nonylphenol polyoxyethylene ether, methanol and propilolic alcohol, four Person's weight ratio is 10:2:6:1.
3. the slow type MH acid system of acidizing sandstone oil reservoir according to claim 1, which is characterized in that the clay is steady Agent is determined for organic ammonium salt and the mixture of ammonium chloride, and the two weight ratio is 3:7;Wherein, organic ammonium salt is 1 by molar ratio:2.5~ 3 ethylenediamine is generated with acetic acid reaction.
4. a kind of acidizing sandstone oil reservoir according to claim 1 construction technology of slow type MH acid system, feature It is, construction procedure is as follows:The sulfamic acid of suitable aqueous solvent and half quality is added in agitator tank first, is stirred evenly After continue to add in organic phospho acid, high-temperature corrosion inhibitor, citric acid, formaldehyde and clay stabilizer into agitator tank, continue stirring to mixed After closing uniformly, gained mixed solution is delivered to underground by casing;After 2~8h is spaced, hydrogen fluoride is added in into agitator tank Amine, the sulfamic acid of remaining half quality and suitable aqueous solvent, well is delivered to after stirring evenly by mixed solution by casing Under.
CN201810055584.0A 2018-01-20 2018-01-20 A kind of acidizing sandstone oil reservoir slow type MH acid system and its construction technology Pending CN108219763A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109777389A (en) * 2019-03-04 2019-05-21 北京国海能源技术研究院 A kind of MH acid system and preparation method thereof suitable for reservoir blockages relieving acidification
CN113046050A (en) * 2021-03-17 2021-06-29 中国海洋石油集团有限公司 Efficient slow-speed acidizing working fluid and preparation method thereof
CN113563864A (en) * 2020-04-29 2021-10-29 中国石油天然气股份有限公司 Sandstone reservoir retarded acid, application and production increase transformation method of sandstone reservoir
CN114427400A (en) * 2020-09-21 2022-05-03 中国石油化工股份有限公司 Method for improving development effect of biological limestone oil reservoir by utilizing acid-producing microorganisms
CN115305079A (en) * 2021-05-08 2022-11-08 中国石油天然气股份有限公司 Alcohol-based multi-hydrogen acid liquid system for sandstone gas reservoir and application thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103074050A (en) * 2011-10-26 2013-05-01 中国石油化工股份有限公司 Anti-scaling multi-hydrogen retarded acid for highly argillaceous sandstone reservoir
CN103642480A (en) * 2013-11-27 2014-03-19 钱程 Novel high-temperature resistant acidification corrosion inhibitor
CN104419393A (en) * 2013-08-30 2015-03-18 周俊 Composite blockage removing fluid
CN105368440A (en) * 2015-12-15 2016-03-02 曲世元 Novel environmental-friendly acidizing fluid suitable for acid-sensitive reservoir stratums, and preparation method thereof
CN105860056A (en) * 2016-04-25 2016-08-17 中国石油集团渤海钻探工程有限公司 Preparation method of high-temperature-resistant clay stabilizer for fracture acidizing

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103074050A (en) * 2011-10-26 2013-05-01 中国石油化工股份有限公司 Anti-scaling multi-hydrogen retarded acid for highly argillaceous sandstone reservoir
CN104419393A (en) * 2013-08-30 2015-03-18 周俊 Composite blockage removing fluid
CN103642480A (en) * 2013-11-27 2014-03-19 钱程 Novel high-temperature resistant acidification corrosion inhibitor
CN105368440A (en) * 2015-12-15 2016-03-02 曲世元 Novel environmental-friendly acidizing fluid suitable for acid-sensitive reservoir stratums, and preparation method thereof
CN105860056A (en) * 2016-04-25 2016-08-17 中国石油集团渤海钻探工程有限公司 Preparation method of high-temperature-resistant clay stabilizer for fracture acidizing

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109777389A (en) * 2019-03-04 2019-05-21 北京国海能源技术研究院 A kind of MH acid system and preparation method thereof suitable for reservoir blockages relieving acidification
CN113563864A (en) * 2020-04-29 2021-10-29 中国石油天然气股份有限公司 Sandstone reservoir retarded acid, application and production increase transformation method of sandstone reservoir
CN114427400A (en) * 2020-09-21 2022-05-03 中国石油化工股份有限公司 Method for improving development effect of biological limestone oil reservoir by utilizing acid-producing microorganisms
CN113046050A (en) * 2021-03-17 2021-06-29 中国海洋石油集团有限公司 Efficient slow-speed acidizing working fluid and preparation method thereof
CN115305079A (en) * 2021-05-08 2022-11-08 中国石油天然气股份有限公司 Alcohol-based multi-hydrogen acid liquid system for sandstone gas reservoir and application thereof

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Application publication date: 20180629

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