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CN106905936B - A kind of substitution CaCl2Alkaline completion fluid and preparation method thereof - Google Patents

A kind of substitution CaCl2Alkaline completion fluid and preparation method thereof Download PDF

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Publication number
CN106905936B
CN106905936B CN201710074054.6A CN201710074054A CN106905936B CN 106905936 B CN106905936 B CN 106905936B CN 201710074054 A CN201710074054 A CN 201710074054A CN 106905936 B CN106905936 B CN 106905936B
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sodium alginate
completion fluid
completion
hydrophobically modified
cacl
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CN106905936A (en
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刘音
张曙光
李立昌
白田增
解洪祥
王红科
王玉忠
刘泸萍
王丹
邱卫红
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China National Petroleum Corp
CNPC Bohai Drilling Engineering Co Ltd
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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
    • C09K8/02Well-drilling compositions
    • C09K8/04Aqueous well-drilling compositions
    • C09K8/06Clay-free compositions
    • C09K8/12Clay-free compositions containing synthetic organic macromolecular compounds or their precursors
    • 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
    • C09K8/02Well-drilling compositions
    • C09K8/04Aqueous well-drilling compositions
    • C09K8/06Clay-free compositions
    • C09K8/08Clay-free compositions containing natural organic compounds, e.g. polysaccharides, or derivatives thereof
    • C09K8/10Cellulose or derivatives thereof

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

The invention discloses a kind of substitution CaCl2Alkaline completion fluid and preparation method thereof, which includes 30~70% potassium carbonate based on mass fraction, 1~3% hydrophobically modified sodium alginate, 1~2% inhibitor, 1~2% fluid loss additive, 0~1% defoaming agent and the water of surplus;By using hydrophobically modified sodium alginate as completion fluid tackifier and the good functional component of environmental-friendly and compatibility for the first time, it is 1.40g/cm that density can be substituted by, which configuring,3CaCl2The novel alkaline completion fluid of completion brine;The alkalinity completion fluid is obtained by stirring evenly the segmentation addition of potassium carbonate, hydrophobically modified sodium alginate, inhibitor, fluid loss additive and defoaming agent into water, and preparation method is simple, and safety has fabulous industrial prospect.

Description

A kind of substitution CaCl2Alkaline completion fluid and preparation method thereof
Technical field
The present invention relates to completion brine technical field, in particular to a kind of substitution CaCl2Alkaline completion fluid and its system Preparation Method.
Background technique
Completion fluid is working solution used in Completion Operations, and major function includes equilibrium strata pressure, carries suspension admittedly Phase particle, raising reservoir protection ability etc..Oil well productivity can be made to reduce by 30% or more using completion fluid inferior, while stratum is made At damage.
CaCl2Completion brine is the Killing Fluid System being commonly used in current Completion Operations, its advantage is that it is cheap, 1.40g/cm can be reached by being completely dissolved rear fluid density3Left and right;However CaCl2There is also many disadvantages for completion brine: 1) In When winter construction, since outdoor temperature is very low (when being lower than 10 DEG C), since the physicochemical property of itself makes CaCl2Solution rate is slow Slowly, solid concentration increases, and saline solution density is extremely difficult to require, and can only achieve 1.25g/cm sometimes3Left and right;2) due to dissolution Property it is poor, inorganic salts insoluble microparticle intrusion causes formation pore to block;3) due to CaCl2For divalent metal salt, Ca2+Salt is easily tied Dirty phenomenon not environmentally has damage to reservoir;4) completion fluid system self performance is short of, and cement particle is made loosely to dissolve afterwards, make mine Object dissolution or recrystallization, occur fine migration and mineral precipitation, cause rock to formation damage.After reservoir is damaged, first is that Be easy to causeing the production capacity of oil reservoirs reduces, and serious person completely loses oil productive capacity, causes the huge economic losses in oil field;Two are intended to It is extremely difficult to be restored to previous level, natural expense is also very expensive.Therefore, it is badly in need of researching and developing a kind of substitution CaCl2 Completion fluid system, reduce the damage to oil-gas Layer to greatest extent.
Summary of the invention
The object of the present invention is to provide one kind can substitute current CaCl2Completion brine is completely dissolved rear fluid density 1.40g/cm can be reached3The alkaline completion fluid of left and right.
Above-mentioned substitution CaCl is prepared it is a further object of the present invention to provide a kind of2Alkaline completion fluid preparation method.
For this purpose, technical solution of the present invention is as follows:
A kind of substitution CaCl2Alkaline completion fluid, including 30~70% potassium carbonate based on mass fraction, 1~3% The water of hydrophobically modified sodium alginate, 1~2% inhibitor, 1~2% fluid loss additive, 0~1% defoaming agent and surplus is (each The sum of constituent content is total 100%).
Wherein, commercial product, industrial goods purity >=95% can be selected in the inorganic salts potassium carbonate;Select potassium carbonate substitution The CaCl that tradition uses2, not only ensure that original CaCl2Completion brine fluid density reaches 1.40g/cm3Requirement;Together When, avoid CaCl2Completion brine is due to Ca2+The problem of reservoir caused by scale formation damages.
Specifically, the hydrophobically modified sodium alginate is to change using alkyl glycidyl ether as raw material to sodium alginate Property be made;Specific step is as follows: weighing a certain amount of sodium alginate and is added into reaction flask, enough water is added to stir to yellow homogeneous Emulsion;Then NaOH is added dropwise and adjusts emulsion pH to 8~9 or so, be slowly added to be equivalent to sodium alginate weight 0.4~ 0.7 times of alkyl glycidyl ether is warming up to 70~80 DEG C and 8~10h of back flow reaction;It is cooled to room temperature, drips after reaction Add acetic acid to adjust reaction solution pH to 3~4, and then enough acetone is added and washes away water and alkyl glycidyl ether in reaction solution, makes Product filters after being precipitated, and washs, and drying is spare.
Wherein, it is 40000~120000 sodium alginate, the alkyl glycidyl that the sodium alginate, which selects molecular weight, Ether one of is but is not limited to octyl glycidyl ether, lauryl diglycidyl ether;It is carried out by alkyl glycidyl ether Hydrophobically modified inhibits the high viscosity characteristic of sodium alginate;By test, sodium alginate after before modified adds in water When entering amount and being 1~1.5wt.%, sodium alginate before modified is slowly dissolved in the viscosity after water and is up to 200mp.s, and passes through and change Property after hydrophobically modified sodium alginate be dissolved in the speed of water and obviously accelerate, viscosity is 120~180mp.s;As it can be seen that hydrophobically modified is extra large Mosanom, which is dissolved in the viscosity after water, effectively to be reduced, while the speed for being dissolved in water is obviously accelerated, that is, enhances water solubility.
It is emphasized that the application is put forward for the first time the thickening using hydrophobically modified sodium alginate as completion fluid system Efficient Adhesive Promotion is being realized in agent, and while effectivelying prevent leakage, faster than other tackifier solution rates, Efficient Adhesive Promotion is more preferable.
The inhibitor polyethylene polyamines, polyaminoacid or modified starch.
Specifically, the polyethylene polyamines are ethylenediamine, diethylenetriamines, trien, tetren Co-product;The polyaminoacid is one of poly-aspartate, polyglutamic acid, polylysine or a variety of;The modified shallow lake Powder is hydroxyethyl modified starch or sodium carboxymethyl starch.
Compared to traditional inhibitor, such as KCl- polyamine salt, above-mentioned inhibitor is without Cl-, because higher without occurring The chloride ion iteration of concentration forms chlorinated compound, and carcinogenic, teratogenesis, mutagens effect, pollution of ecological environment occurs.
The fluid loss additive is carboxymethyl cellulose;Carboxymethyl cellulose not only has filtrate loss controllability, also belongs to simultaneously Modified natural polymer is environmental-friendly degradation material.
The defoaming agent is dimethyl silicone polymer, polyoxyethylene polyoxy propyl alcohol amidogen ether or polypropylene glycerol aether;
A kind of substitution CaCl2Alkaline completion fluid preparation method, steps are as follows: by deionized water, 30~70% nothing Machine salt potassium carbonate, 1~2% inhibitor, 1~2% fluid loss additive are added sequentially to stir evenly in reaction flask, stir at room temperature Mix 0.5~1h, then be added 1~3% hydrophobically modified sodium alginate, continue at room temperature stirring 0.5~1h to be uniformly mixed, It is eventually adding 0~1% defoaming agent, continues stirring until forming uniform alkaline completion fluid system;Wherein, above-mentioned each component plus Enter amount based on mass fraction, the sum of the additional amount of deionized water and other each component additional amounts are 100%.The hydrophobically modified Sodium alginate is modified to sodium alginate obtained using alkyl glycidyl ether as raw material.
The alkalinity completion fluid system is transparency liquid, and pH is 10~12.
Compared with prior art, substitution CaCl2The alkaline completion fluid of completion brine select potassium carbonate as monovalence without Machine salt prepares alkaline completion fluid, and good by dissolubility, solution rate is fast, non-scaling, and environmental protection is small to reservoir damage, after dissolution Density of completion fluids can reach 1.40g/cm3Etc. outstanding features, be configured to new potassium carbonate salt water completion fluid system, realize complete Substitute tradition CaCl2Completion brine;In addition, the alkalinity completion fluid system filters out compatibility well and has environmental-friendly spy Property hydrophobically modified sodium alginate, inhibitor, fluid loss additive and defoaming agent, make, Low Damage pollution-free to reservoir, and construct Middle use is safe, not only balances strata pressure, but also protect the novel alkaline completion fluid of oil and gas reservoir;In addition, substitution CaCl2 The alkaline completion fluid preparation method of completion brine is simple, and safety has fabulous industrial prospect.
Specific embodiment
The present invention is described further combined with specific embodiments below, but following embodiments absolutely not to the present invention have appoint What is limited.
In following Examples 1 to 4, potassium carbonate (industrial goods purity >=95%), poly-aspartate, polyethylene polyamines, carboxylic Methylcellulose, dimethyl silicone polymer, hydroxyethyl modified starch and polypropylene glycerol aether are purchased from commercial product;It is hydrophobic Modified sodium alginate is prepared by laboratory.
Specifically, hydrophobically modified sodium alginate is added to reaction flask the preparation method comprises the following steps: weighing a certain amount of sodium alginate In, add enough water to stir to the emulsion of yellow homogeneous;Then NaOH is added dropwise and adjusts emulsion pH to 9 or so, is slowly added to phase When in 0.5 times of sodium alginate weight of octyl glycidyl ether, being warming up to 75 DEG C and back flow reaction 8h;It is cooled to after reaction Room temperature is added dropwise acetic acid and adjusts reaction solution pH to 4, and then enough acetone is added and washes away water and octyl glycidyl in reaction solution Ether filters, acetone secondary washing after product is precipitated, and drying is spare.
Embodiment 1
54.2 parts of deionized waters, 40 parts of potassium carbonate, 1 part of poly-aspartate, 1.8 parts of carboxymethyl celluloses are added sequentially to It is stirred evenly in reaction flask, and 0.5~1h is stirred at room temperature;Then 2.5 parts of hydrophobically modified alginic acids are added into reaction flask Sodium continues 0.5~1h of stirring, makes mixed system uniform state;And then 0.5 part of polyoxypropylene glyceryl is added into reaction flask Ether continues stirring until forming uniform transparent basic completion fluid system.
Wherein, the addition number of above-mentioned each component is parts by weight, and following example 2~5 are same, is repeated no more.
Embodiment 2
40.5 parts of deionized waters, 55 parts of potassium carbonate, 1.5 parts of polyethylene polyamines, 1.2 parts of carboxymethyl celluloses are sequentially added It is stirred evenly into reaction flask, and 0.5~1h is stirred at room temperature;Then 1.5 parts of hydrophobically modified seaweed are added into reaction flask Sour sodium continues 0.5~1h of stirring, makes mixed system uniform state;And then 0.3 part of polydimethylsiloxanes is added into reaction flask Alkane continues stirring until forming uniform transparent basic completion fluid system.
Embodiment 3
27.6 parts of deionized waters, 65 parts of potassium carbonate, 2 parts of hydroxyethyl modified starch, 1.5 parts of carboxymethyl celluloses are successively added Enter and stirred evenly into reaction flask, and 0.5~1h is stirred at room temperature;Then 3 parts of hydrophobically modified seaweed are added into reaction flask Sour sodium continues 0.5~1h of stirring, makes mixed system uniform state;And then 0.9 part of polyoxypropylene glyceryl is added into reaction flask Ether continues stirring until forming uniform transparent basic completion fluid system.
Embodiment 4
48.7 parts of deionized waters, 47 parts of potassium carbonate, 1.2 parts of polyethylene polyamines, 2 parts of carboxymethyl celluloses are added sequentially to It is stirred evenly in reaction flask, and 0.5~1h is stirred at room temperature;Then 1 part of hydrophobically modified sodium alginate is added into reaction flask, Continue 0.5~1h of stirring, makes mixed system uniform state;And then 0.1 part of polyoxyethylene polyoxy propyl alcohol is added into reaction flask Amidogen ether continues stirring until forming uniform transparent basic completion fluid system.
The relevant nature of the alkaline completion fluid system of Examples 1 to 4 preparation is tested, test includes liquid pH value Measurement, fluid density measurement are with, compatibility and the experiment of core permeability recovery value and core damage rate evaluation experimental.
Wherein, core permeability recovery value be evaluation completion fluid to the extent of damage of reservoir or to reservoir protection effect most Intuitive method;It uses natural core in flooding test device, the permeability of measurement experiment rock core pollution front and back, gained ratio Value is permeability resume figure.Permeability resume figure can intuitively reflect the extent of damage of reservoir core.The permeability of completion fluid Recovery value is bigger, illustrates smaller to formation damage, and general permeability resume figure should (specific method can refer to " sand not less than 75% Rock reservoir sensitivity evaluation --- core flow test program " professional standard).
The measuring method of core damage rate: it takes several blocks of rock cores that washing oil, the desalinization of soil by flooding or leaching have been handled to do parallel laboratory test, uses coal first The original permeability of oil every block of rock core of test, then pollutes rock core using the alkaline completion fluid of preparation, re-test pollution Core permeability afterwards evaluates core damage rate by the ratio of the permeability of pollution front and back.
Test result is as follows shown in table 1.
Table 1:
From the test result of upper table 1 can be seen that Examples 1 to 4 prepare carry out compounding alkali by inorganic salts of potassium carbonate The property completion fluid system equal > 10 of pH, density can reach 1.39~1.47g/cm3, it is fully able to substitute traditional calcium chloride brine complete Well liquid system;In addition, introducing completion fluid system as tackifier for by the sodium alginate of hydrophobically modified, and pass through many experiments Filter out with excellent degradability and with substance as inhibitor, fluid loss additive and defoaming agent and potassium carbonate and hydrophobically modified The completion fluid that sodium alginate is configured is uniformly dissolved, and compatibility is good.
In addition, the alkalinity completion fluid is in core permeability recovery value and the test of core damage rate, core permeability is extensive Complex value is more than 80, and core damage rate controls below 20.1%;And the formation damage for comparing calcium chloride brine completion fluid system is commented The core permeability recovery value of valence experimental result, calcium chloride brine completion fluid is about 75, and core damage rate is about 25%, it is seen that this The disclosed alkaline completion fluid of application not only can achieve the effect of traditional calcium chloride brine completion fluid system, and can be maximum Limit reduces the damage to oil-gas Layer.

Claims (3)

1. a kind of substitution CaCl2Alkaline completion fluid, which is characterized in that including 30~70% potassium carbonate based on mass fraction, 1~3% hydrophobically modified sodium alginate, 1~2% inhibitor, 1~2% fluid loss additive, 0~1% defoaming agent and surplus Water, the sum of each component content total 100%;Wherein, the inhibitor is polyethylene polyamines, polyaminoacid or modified starch; The hydrophobically modified sodium alginate is the sodium alginate for being 40000~120000 to molecular weight by raw material of alkyl glycidyl ether It is modified hydrophobically modified sodium alginate obtained;The fluid loss additive is carboxymethyl cellulose;The polyethylene polyamines are second The co-product of diamines, diethylenetriamines, trien, tetren;The polyaminoacid be poly-aspartate, One of polyglutamic acid, polylysine are a variety of;The modified starch is hydroxyethyl modified starch or the carboxymethyl modified shallow lake of sodium Powder.
2. substitution CaCl according to claim 12Alkaline completion fluid, which is characterized in that the defoaming agent be poly dimethyl Siloxanes, polyoxyethylene polyoxy propyl alcohol amidogen ether or polypropylene glycerol aether.
3. a kind of substitution CaCl as described in claim 12Alkaline completion fluid preparation method, which is characterized in that step is such as Under: by deionized water, 30~70% inorganic salts potassium carbonate, 1~2% inhibitor, 1~2% fluid loss additive sequentially add It is stirred evenly into reaction flask, stirs 0.5~1h at room temperature, 1~3% hydrophobically modified sodium alginate is then added, continues room Lower 0.5~the 1h of stirring of temperature is eventually adding 0~1% defoaming agent to being uniformly mixed, and continues stirring until forming the uniform complete well of alkalinity Liquid system;Wherein, based on mass fraction, the additional amount of deionized water and other each components are added the additional amount of above-mentioned each component The sum of amount is 100%.
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Citations (2)

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Publication number Priority date Publication date Assignee Title
CN1342189A (en) * 1999-02-09 2002-03-27 Masi科技股份有限公司 Aphron-containing aqueous well drilling and servicing fluids
WO2016072993A1 (en) * 2014-11-06 2016-05-12 Halliburton Energy Services, Inc. Composition including a viscosifier and a hydrophobically-modified polymer that includes a nitrogen-containing repeating unit for treatment of subterranean formations

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US10155897B2 (en) * 2013-08-16 2018-12-18 Hilliburton Energy Services, Inc. Hydrophobically and hydrophilically modified polysaccharides and methods of using the same for treatment of a subterranean formation

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1342189A (en) * 1999-02-09 2002-03-27 Masi科技股份有限公司 Aphron-containing aqueous well drilling and servicing fluids
WO2016072993A1 (en) * 2014-11-06 2016-05-12 Halliburton Energy Services, Inc. Composition including a viscosifier and a hydrophobically-modified polymer that includes a nitrogen-containing repeating unit for treatment of subterranean formations

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Inventor after: Liu Yin

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