CN102464976B - Oil-displacing composition and preparation method thereof - Google Patents
Oil-displacing composition and preparation method thereof Download PDFInfo
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- CN102464976B CN102464976B CN201010552246.1A CN201010552246A CN102464976B CN 102464976 B CN102464976 B CN 102464976B CN 201010552246 A CN201010552246 A CN 201010552246A CN 102464976 B CN102464976 B CN 102464976B
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Abstract
The invention relates to an oil-displacing composition and a preparation method thereof, which mainly solve the problems in the prior art that the oil-displacing agent comprising polymer has poor temperature resistance, poor salt resistance and low oil displacement efficiency. The oil-displacing composition comprises the following ingredients by weight percent: (1) 0.01 to 3 percent of oil-displacing inorganic nanocomposite polyacrylamide, (2) 0.01 to 5 percent of fatty alcohol polyoxyethylene ether carboxylate surface active agent and (3) 92 to 99.98 percent of oil field injection water, wherein the ingredient (1), i.e. the oil-displacing inorganic nanocomposite polyacrylamide comprises the following ingredients in parts by weight: a) 1 to 10 parts of inorganic nanometer material which is selected from carbon nano pipes, nano zinc oxide, nano silicon oxide or nano titanium oxide, and b) 90 to 99 parts of polyacrylamide; and the molecular formula of the ingredient (2) is RO(CH2CH2O)nCH2COOM, wherein in the formula: R is alkyl of C12 to C18, n is an adding number of ethoxy group EO and is an integer of 2 to 8. The oil-displacing composition can well solve the problems and can be used in the tertiary recovery of an oil field.
Description
Technical field
The present invention relates to a kind of displacement of reservoir oil composition and method of making the same.
Background technology
Oil is a kind of important energy and industrial chemicals, is also national grand strategy goods and materials simultaneously, and the development of national economy is had to very important impact, have the title of " industry blood ".Oil, as a kind of deregenerative fossil energy, be the topmost a kind of energy using at present, and consumption shared ratio in total energy increases year by year.Oil recovery is not only petroleum industrial circle, and is the problem that entire society is generally concerned about.The problem that oil production at present faces has one, and imbalance between supply and demand is outstanding, and petroleum demand amount is more larger, and find is fewer and feweri; Two, also left in exhausted oil reservoir have a substantial oil.Primary oil recovery can the underground crude oil of extraction 10～25%, and secondary oil recovery can the underground crude oil of extraction 15～25%, i.e. a primary oil recovery and secondary oil recovery extraction 25～50% underground crude oil.In order to guarantee oil supply steady in a long-term, to meet human wants, must research and development improve petroleum recovery technology, tertiary oil recovery, by intensified oil reduction measure, can make oil recovery factor improve 6～20% again, even more.Polymer flooding is the main technique methods of tertiary oil recovery, and oil-displacement mechanism is clear, and technique is relatively simple, and technology reaches its maturity, and is one and effectively improves recovery efficiency technique measure.The oil-displacement mechanism of polymkeric substance is mainly the viscosity of utilizing water-soluble polyacrylamide molecular chain, improves the mobility ratio of displacing fluid, improves efficiency of displacement and swept volume, thereby reaches the object that improves recovery ratio.
Document CN1865299, CN1498908A, CN1746198, CN101157736A, CN1542027, CN101029107, CN101029099 and CN101514240A are from the initiator system of polyacrylamide polymerization, several respects of polymerization process and method for hydrolysis are studied, although had larger improvement improving aspect the molecular weight of anion-polyacrylamide or dissolution rate by all means, but in the less concern of temperature resistant antisalt aspect of performance, but these preparation methods are comparatively complicated, processing condition are harsh, the temperature resistant antisalt performance of polymkeric substance is also difficult to reach the technical indicator of used for tertiary oil recovery acrylamide copolymer.
Summary of the invention
To be the existing displacement of reservoir oil there is temperature resistant antisalt poor performance, problem that oil displacement efficiency is low with composition to one of technical problem to be solved by this invention, a kind of displacement of reservoir oil composition is provided, it is low that this displacement of reservoir oil has working concentration with composition, the high feature of oil displacement efficiency under high temperature and high salt condition.Two of technical problem to be solved by this invention is to provide the preparation method of composition for a kind of displacement of reservoir oil corresponding with one of technical solution problem.
In order one of to solve the problems of the technologies described above, the technical solution used in the present invention is as follows: a kind of displacement of reservoir oil composition, comprises following component by weight percentage:
(1) 0.01～3.0% inorganic nanocomposite polyacrylamide for displacing reservoir oil;
(2) 0.01～5.0% aliphatic alcohol polyethenoxy ether carboxylate tensio-active agent;
(3) 92.0～99.98% oilfield injection water;
Wherein (1) component inorganic nanocomposite polyacrylamide for displacing reservoir oil comprises following component in weight fraction:
A) 1～10 part of inorganic nano material is selected from carbon nanotube, nano zine oxide, nano silicon oxide or nano-titanium oxide;
B) 90～99 parts of polyacrylamides.
In technique scheme, described tensio-active agent is selected from aliphatic alcohol polyethenoxy ether carboxylate type the moon-nonsurfactant, and general molecular formula is RO (CH
2cH
2o)
ncH
2cOOM; In described aliphatic alcohol polyethenoxy ether carboxylate, the carbonatoms of R is that 12～18, n is the adduction number of ethoxy group EO, is selected from any one integer in 2～8, and metal ions M is selected from potassium, sodium or lithium.
For solve the problems of the technologies described above two, the technical solution used in the present invention is as follows: the preparation method of composition for a kind of displacement of reservoir oil, comprises the following steps:
A) acrylamide monomer of aequum being made into mass concentration is 10～40% water solution A;
B) to the inorganic nano material that adds acrylamide monomer weight 0.1～10% in solution A, obtain solution B;
C) solution B is put into ultrasonic pond, ultrasonic 10～60 minutes, and letting nitrogen in and deoxidizing 10～40 minutes simultaneously;
D) add the composite initiation system: compositions with respect to monomer mass concentration 0.02～5%, obtain solution C;
E) to letting nitrogen in and deoxidizing in solution C, after 10～40 minutes, at 5～25 ℃, cause, polymerization after 2～10 hours gluey product A;
F) add the reaction 1～5 hour that is hydrolyzed of the alkali lye of mass concentration 5～50% after gluey product A is shredded, wherein temperature is 80～95 ℃, obtains gluey product B;
G) by gluey product B drying, after pulverizing, sieving the inorganic nano combined polyacrylamide of fine particulate;
H) the inorganic nano combined polyacrylamide of aequum, above-mentioned aliphatic alcohol polyethenoxy ether carboxylate and injected water are evenly mixed, 5～35 ℃ are stirred 1～3 hour, obtain required composition, by weight percentage, the proportioning of anion-polyacrylamide, aliphatic alcohol polyethenoxy ether carboxylate and injected water is 0.01～3.0%: 0.01～5.0%: 92.0～99.98;
Wherein composite initiation system: compositions, comprises following component: (a) 0.5～20% persulphate by weight percentage; (b) 0.1～40% sulphite; (c) 0.5～20% by NR
1r
2r
3representative tertiary amine compounds or by N
+r
4r
5r
6r
7representative quaternary ammonium compounds or by NH
2r
8the fat amine compound of representative, R in formula
1～R
7all be selected from C
1～C
14straight or branched alkyl or alkyl derivative, R
8be selected from C
1～C
17straight or branched alkyl or alkyl derivative.
The displacement of reservoir oil composition that the present invention is prepared, owing to having adopted inorganic nano combined polyacrylamide, because its inorganic nano component is evenly dispersed in and forms ultra-fine structure phase in polyacrylamide matrix with nano-scale or molecular level, the character of its matrix material all has greatly improved than its corresponding macroscopic view or micron order matrix material, can effectively improve the temperature resistant antisalt performance of Polyacrylamides For Enhanced Oil Recoveries.The present invention has realized the dispersed of inorganic nano material by the method for ultrasonic dispersion, then by in-situ polymerization, inorganic nano material is introduced in Polymer Used For Oil Displacement, prepared inorganic nanocomposite polyacrylamide for displacing reservoir oil, at three times, adopted in application and obtained good technique effect.
The inorganic nano combined polyacrylamide that adopts the present invention to prepare, the aliphatic alcohol polyethenoxy ether carboxylate tensio-active agent that the consumption of take is 0.1～0.3wt% and 0.1～0.4wt% forms displacement of reservoir oil composition, under alkali-free condition, the in-place oil and the water that can be used for the oil field block of comparatively high temps and salinity, measured the solution apparent viscosity of this oil-displacing agent at 85 ℃ of Shengli Oil Field Sheng Tuo bis-district's Simulated Water, be greater than 18mPa.s, and the dynamic interface tension value between Shengli Oil Field Sheng Tuo bis-district's crude oil, can reach 10
-3～10
-4the ultra low interfacial tension of mN/m, through physical simulation displacement test Lab-evaluation this oil-displacing agent on high temperature, high salinity reservoir, can on water drive basis, can reach 17.6% by (water drive improves oil recovery factor and reaches 40.6%) raising oil recovery factor, obtain good technique effect.
Below by embodiment, the present invention is further illustrated.Be necessary to be pointed out that at this following examples, only for further illustrating of the present invention, can not be interpreted as limiting the scope of the invention.Below by embodiment, the present invention is further elaborated.
Embodiment
[embodiment 1]
125g acrylamide (AM) is added in 350g deionized water, after stirring and dissolving is even, with the NaOH solution of 5% mass concentration, regulate pH value to 8, add 0.125g carbon nanotube, ultrasonic and to control bath temperature be 15 ℃, pass into high pure nitrogen simultaneously, after ultrasonic logical nitrogen 30min, add successively 1.25% methacrylic acid N, N-dimethylaminoethyl (DMAEMA) aqueous solution 1g, 1.25% persulfate aqueous solution 1g, 1% aqueous solution of sodium bisulfite 1g, after 1 hour, temperature of reaction is risen to 40 ℃ gradually, react and obtain gel polymerisate after 5 hours, after cutting glue, add 10%NaOH aqueous solution 140g, 90 ℃ of hydrolysis reaction 2 hours, then vacuum-drying 6h at 75 ℃, with pulverizer, smash the rear sampling analysis of screening.
By GB/T12005.2-89 polyacrylamide determination of solid content method test solid content, be 90.5%, press GB/T12005.8-89 powdered polypropylene acid amides measuring of dissolution velocity method test dissolution time≤90min, by GB/T12005.6-89 partially hydrolyzed polyacrylamide degree of hydrolysis measuring method test degree of hydrolysis, be 20.6%, press GB/T12005.10-92 Molecular Weight for Polyacrylamide and measure (viscosimetry) mensuration intrinsic viscosity, and by [η]=3.73 * 10
-4mw
0.66calculating molecular weight is that 2,980 ten thousand, 1500mg/L polymer concentration solution are at 85 ℃, 7.34s
-1under apparent viscosity be 19.6mPas (salt solution total mineralization 19334mgL
-1, Ca
2++ Mg
2+: 514mgL
-1).
The inorganic nano combined polyacrylamide 0.15wt% of synthesized, above-mentioned aliphatic alcohol polyethenoxy ether carboxylate (n=4) 0.25wt% and 99.6wt% Shengli Oil Field Sheng Tuo bis-district's victory injected waters are evenly mixed, 20 ℃ are stirred 2 hours, obtain required displacement of reservoir oil composition.At 85 ℃ of temperature, salinity 19334mg/L, Ca
2++ Mg
2+in the water of 514mg/L, the apparent viscosity that records this composition is 20.5mPa.s.; Between said composition and Shengli Oil Field Sheng Tuo bis-district 0-141 well dewatered oils, form the ultra low interfacial tension of 0.0058mN/m.Apparent viscosity is by the BROOKFIELDIII type viscometer determining of U.S. Brookfield company, and the TX500 type rotation interfacial tensimeter that interfacial tension is produced by Texas ,Usa university is measured.
[embodiment 2]
First 125g acrylamide (AM) is added in 370g deionized water, after stirring and dissolving is even, with the NaOH solution of 5% mass concentration, regulate pH value to 8, add 0.125g nano zine oxide, ultrasonic and to control bath temperature be 15 ℃, pass into high pure nitrogen simultaneously, after ultrasonic logical nitrogen 30min, add successively 1.25% β-dimethylaminopropionitrile aqueous solution 1g, 1.25% sodium persulfate aqueous solution 1g, 1.69% potassium sulfite aqueous solution 1g, after 1 hour, temperature of reaction is risen to 40 ℃ gradually, react and obtain gel polymerisate after 5 hours, after cutting glue, add 10%NaOH aqueous solution 140g, 90 ℃ of hydrolysis reaction 2 hours, then vacuum-drying 6h at 75 ℃, with pulverizer, smash the rear sampling analysis of screening.
By GB/T12005.2-89 polyacrylamide determination of solid content method test solid content, be 89.9%, press GB/T12005.8-89 powdered polypropylene acid amides measuring of dissolution velocity method test dissolution time≤120min, by GB/T12005.6-89 partially hydrolyzed polyacrylamide degree of hydrolysis measuring method test degree of hydrolysis, be 22.1%, press GB/T12005.10-92 Molecular Weight for Polyacrylamide and measure (viscosimetry) mensuration intrinsic viscosity, and by [η]=3.73 * 10
-4mw
0.66calculating molecular weight is that 2,362 ten thousand, 1500mg/L polymer concentration solution are at 85 ℃, 7.34s
-1under apparent viscosity be 18.2mPas (salt solution total mineralization 19334mgL
-1, Ca
2++ Mg
2+: 514mgL
-1).
The inorganic nano combined polyacrylamide 0.15wt% of synthesized, above-mentioned aliphatic alcohol polyethenoxy ether carboxylate (n=4) 0.25wt% and 99.6wt% Shengli Oil Field Sheng Tuo bis-district's victory injected waters are evenly mixed, 20 ℃ are stirred 2 hours, obtain required displacement of reservoir oil composition.At 85 ℃ of temperature, salinity 19334mg/L, Ca
2++ Mg
2+in the water of 514mg/L, the apparent viscosity that records this composition is 18.8mPa.s.; Between said composition and Shengli Oil Field Sheng Tuo bis-district 0-141 well dewatered oils, form the ultra low interfacial tension of 0.0043mN/m.Apparent viscosity is by the BROOKFIELDIII type viscometer determining of U.S. Brookfield company, and the TX500 type rotation interfacial tensimeter that interfacial tension is produced by Texas ,Usa university is measured.
[embodiment 3]
First 125g acrylamide (AM) is added in 370g deionized water, after stirring and dissolving is even, with the NaOH solution of 5% mass concentration, regulate pH value to 8, add 0.125g carbon nanotube, ultrasonic and to control bath temperature be 15 ℃, pass into high pure nitrogen simultaneously, after ultrasonic logical nitrogen 30min, add successively 1.25% methacrylic acid N, N-dimethylaminoethyl (DMAEMA) aqueous solution 1g, 1.25% ammonium persulfate aqueous solution 1g, 2.63% bisulfite aqueous solutions of potassium 1g, after 1 hour, temperature of reaction is risen to 40 ℃ gradually, react and obtain gel polymerisate after 5 hours, after cutting glue, add 10%NaOH aqueous solution 140g, 90 ℃ of hydrolysis reaction 2 hours, then vacuum-drying 6h at 75 ℃, with pulverizer, smash the rear sampling analysis of screening.
By GB/T12005.2-89 polyacrylamide determination of solid content method test solid content, be 89.8%, press GB/T12005.8-89 powdered polypropylene acid amides measuring of dissolution velocity method test dissolution time≤90min, by GB/T12005.6-89 partially hydrolyzed polyacrylamide degree of hydrolysis measuring method test degree of hydrolysis, be 19.6%, press GB/T12005.10-92 Molecular Weight for Polyacrylamide and measure (viscosimetry) mensuration intrinsic viscosity, and by [η]=3.73 * 10
-4mw
0.66calculating molecular weight is that 2,501 ten thousand, 1500mg/L polymer concentration solution are at 85 ℃, 7.34s
-1under apparent viscosity be 18.6mPas (salt solution total mineralization 19334mgL
-1, Ca
2++ Mg
2+: 514mgL
-1).
The inorganic nano combined polyacrylamide 0.15wt% of synthesized, above-mentioned aliphatic alcohol polyethenoxy ether carboxylate (n=4) 0.25wt% and 99.6wt% Shengli Oil Field Sheng Tuo bis-district's victory injected waters are evenly mixed, 20 ℃ are stirred 2 hours, obtain required displacement of reservoir oil composition.At 85 ℃ of temperature, salinity 19334mg/L, Ca
2++ Mg
2+in the water of 514mg/L, the apparent viscosity that records this composition is 19.2mPa.s.; Between said composition and Shengli Oil Field Sheng Tuo bis-district 0-141 well dewatered oils, form the ultra low interfacial tension of 0.0065mN/m.Apparent viscosity is by the BROOKFIELDIII type viscometer determining of U.S. Brookfield company, and the TX500 type rotation interfacial tensimeter that interfacial tension is produced by Texas ,Usa university is measured.
[embodiment 4]
First 125g acrylamide (AM) is added in 369g deionized water, after stirring and dissolving is even, with the NaOH solution of 5% mass concentration, regulate pH value to 8, and water-bath is cooled to 15 ℃, then start to pass into high pure nitrogen, after logical nitrogen 30min, add successively 1.56% methacrylic acid N, N-dimethylaminoethyl (DMAEMA) aqueous solution 1g, 1.25% ammonium persulfate aqueous solution 1g, 0.94% sodium sulfite aqueous solution 1g, after 1 hour, temperature of reaction is risen to 40 ℃ gradually, react and obtain gel polymerisate after 5 hours, after cutting glue, add 10%NaOH aqueous solution 140g, 90 ℃ of hydrolysis reaction 2 hours, then vacuum-drying 6h at 75 ℃, with pulverizer, smash the rear sampling analysis of screening.
By GB/T12005.2-89 polyacrylamide determination of solid content method test solid content, be 89.8%, press GB/T12005.8-89 powdered polypropylene acid amides measuring of dissolution velocity method test dissolution time≤90min, by GB/T12005.6-89 partially hydrolyzed polyacrylamide degree of hydrolysis measuring method test degree of hydrolysis, be 21.4%, press GB/T12005.10-92 Molecular Weight for Polyacrylamide and measure (viscosimetry) mensuration intrinsic viscosity, and by [η]=3.73 * 10
-4mw
0.66calculating molecular weight is that 2,835 ten thousand, 1500mg/L polymer concentration solution are at 85 ℃, 7.34s
-1under apparent viscosity be 19.2mPas (salt solution total mineralization 19334mgL
-1, Ca
2++ Mg
2+: 514mgL
-1).
The inorganic nano combined polyacrylamide 0.15wt% of synthesized, above-mentioned aliphatic alcohol polyethenoxy ether carboxylate (n=4) 0.25wt% and 99.6wt% Shengli Oil Field Sheng Tuo bis-district's victory injected waters are evenly mixed, 20 ℃ are stirred 2 hours, obtain required displacement of reservoir oil composition.At 85 ℃ of temperature, salinity 19334mg/L, Ca
2++ Mg
2+in the water of 514mg/L, the apparent viscosity that records this composition is 19.8mPa.s.; Between said composition and Shengli Oil Field Sheng Tuo bis-district 0-141 well dewatered oils, form the ultra low interfacial tension of 0.0052mN/m.Apparent viscosity is by the BROOKFIELDIII type viscometer determining of U.S. Brookfield company, and the TX500 type rotation interfacial tensimeter that interfacial tension is produced by Texas ,Usa university is measured.
[embodiment 5～8]
By the synthetic inorganic nano combined polyacrylamide of embodiment 1～4, the aliphatic alcohol polyethenoxy ether carboxylate tensio-active agent that the consumption of take is 0.1～0.3wt% and 0.1～0.4wt% forms displacement of reservoir oil composition, under alkali-free condition, measured the solution apparent viscosity of this oil-displacing agent at 85 ℃ of Shengli Oil Field Sheng Tuo bis-district's Simulated Water, be greater than 18mPa.s, and the dynamic interface tension value between Shengli Oil Field Sheng Tuo bis-district's crude oil, can reach 10
-3～10
-4the ultra low interfacial tension of mN/m; In length, be 30 centimetres, diameter is 2.5 centimetres, and rate of permeation is 1.5 microns
2rock core on carry out physical simulation displacement test, Lab-evaluation this oil-displacing agent on high temperature, high salinity reservoir can reach 16.2～17.6% by (water drive can improve oil recovery factor 40.1～40.8%) raising oil recovery factor on water drive basis, the results are shown in Table shown in 1.The TX500 type rotation interfacial tensimeter that interfacial tension is produced by Texas ,Usa university is measured.
[comparative example 1]
125g acrylamide monomer is added in 355g deionized water, stir after dissolving completely, NaOH solution with 5% regulates pH value to 8, then lead to nitrogen 30min, and bath temperature is adjusted to 15 ℃, add respectively 1.25% methacrylic acid N, N-dimethylaminoethyl (DMAEMA) aqueous solution 1g, the persulfate aqueous solution 1g of 1.25wt%, the aqueous solution of sodium bisulfite 1g of 0.963wt%, after 30min, temperature of reaction is risen to 40 ℃ gradually, after reaction 5h, take out blob of viscose, be ground into after particulate state, add 140 grams of 10% the NaOH aqueous solution, hydrolysis reaction 2h at 90 ℃, then under 75 ℃ of vacuum, be dried 6h, with pulverizer, smash the rear sampling analysis of screening.
By GBT12005.2-89 polyacrylamide determination of solid content method test solid content, be 88.65%, by GBT12005.6-89 partially hydrolyzed polyacrylamide degree of hydrolysis measuring method test degree of hydrolysis, be 20.3%, press GBT12005.10-92 Molecular Weight for Polyacrylamide and measure (viscosimetry) mensuration intrinsic viscosity, and by [η]=3.73 * 10
-4mw
0.66calculating molecular weight is 1,986 ten thousand, and in the aqueous solution that total mineralization is 19334mg/L, wherein the total amount of calcium ion and magnesium ion is 514mg/L, 1500mg/L polymer concentration solution is at 85 ℃, 7.34s
-1under apparent viscosity be 10.2mps.
The above-mentioned displacement of reservoir oil composition making carries out the displacement of reservoir oil with the method for same embodiment 5, records water drive and can improve oil recovery factor 40.2%, after the above-mentioned displacement of reservoir oil composition of metaideophone, can on water drive basis, improve oil recovery factor 10.9% again, the results are shown in Table shown in 1.
[comparative example 2]
125g acrylamide monomer is added in 345g deionized water, stir after dissolving completely, NaOH solution with 5% regulates pH value to 8, then lead to nitrogen 30min, and bath temperature is adjusted to 15 ℃, the persulfate aqueous solution 10g that adds respectively 0.125wt%, the aqueous solution of sodium bisulfite 10g of 0.0963wt%, the AIBI aqueous solution 10g of 0.125wt%, after 30min, temperature of reaction is risen to 40 ℃ gradually, after reaction 5h, take out blob of viscose, be ground into after particulate state, add 140 grams of 10% the NaOH aqueous solution, hydrolysis reaction 2h at 90 ℃, then under 75 ℃ of vacuum, be dried 6h, with pulverizer, smash the rear sampling analysis of screening.
By GBT12005.2-89 polyacrylamide determination of solid content method test solid content, be 87.54%, by GBT12005.6-89 partially hydrolyzed polyacrylamide degree of hydrolysis measuring method test degree of hydrolysis, be 21.32%, press GBT12005.10-92 Molecular Weight for Polyacrylamide and measure (viscosimetry) mensuration intrinsic viscosity, and by [η]=3.73 * 10
-4mw
0.66calculating molecular weight is 2,182 ten thousand, and in the aqueous solution that total mineralization is 19334mg/L, wherein the total amount of calcium ion and magnesium ion is 514mg/L, 1500mg/L polymer concentration solution is at 85 ℃, 7.34s
-1under apparent viscosity be 10.9mps.
The above-mentioned displacement of reservoir oil composition making carries out the displacement of reservoir oil with the method for same embodiment 5, records water drive and can improve oil recovery factor 40.5%, after the above-mentioned displacement of reservoir oil composition of metaideophone, can on water drive basis, improve oil recovery factor 11.2% again, the results are shown in Table shown in 1.
Claims (2)
1. a displacement of reservoir oil composition, comprises following component by weight percentage:
(1) 0.01～3.0% inorganic nanocomposite polyacrylamide for displacing reservoir oil;
(2) 0.01～5.0% aliphatic alcohol polyethenoxy ether carboxylate tensio-active agent;
(3) 92.0～99.98% oilfield injection water;
Wherein, (1) component inorganic nanocomposite polyacrylamide for displacing reservoir oil comprises following component in weight fraction:
A) 1～10 part of inorganic nano material is selected from carbon nanotube, nano zine oxide, nano silicon oxide or nano-titanium oxide;
B) 90～99 parts of polyacrylamides;
(2) component aliphatic alcohol polyethenoxy ether carboxylate tensio-active agent is aliphatic alcohol polyethenoxy ether carboxylate type the moon-nonsurfactant, and general molecular formula is RO (CH
2cH
2o)
ncH
2cOOM; Wherein the carbonatoms of R is that 12～18, n is the adduction number of ethoxy group EO, is selected from any one integer in 2～8, and metal ions M is selected from potassium, sodium or lithium.
2. the preparation method of composition for the displacement of reservoir oil according to claim 1, comprises the following steps:
A) acrylamide monomer of aequum being made into mass concentration is 10～40% water solution A;
B) to the inorganic nano material that adds acrylamide monomer weight 0.1～10% in solution A, obtain solution B;
C) solution B is put into ultrasonic pond, ultrasonic 10～60 minutes, and letting nitrogen in and deoxidizing 10～40 minutes simultaneously;
D) add the composite initiation system: compositions with respect to monomer mass concentration 0.02～5%, obtain solution C;
E) to letting nitrogen in and deoxidizing in solution C, after 10～40 minutes, at 5～25 ℃, cause, polymerization after 2～10 hours gluey product A;
F) add the reaction 1～5 hour that is hydrolyzed of the alkali lye of mass concentration 5～50% after gluey product A is shredded, wherein temperature is 80～95 ℃, obtains gluey product B;
G) by gluey product B drying, after pulverizing, sieving the inorganic nano combined polyacrylamide of fine particulate;
H) the inorganic nano combined polyacrylamide of aequum, above-mentioned aliphatic alcohol polyethenoxy ether carboxylate and injected water are evenly mixed, 5～35 ℃ are stirred 1～3 hour, obtain required composition;
Wherein composite initiation system: compositions, comprises following component: (a) 0.5～20% persulphate by weight percentage; (b) 0.1～40% sulphite; (c) 0.5～20% by NR
1r
2r
3representative tertiary amine compounds or by N
+r
4r
5r
6r
7representative quaternary ammonium compounds or by NH
2r
8the fat amine compound of representative, R in formula
1～R
7all be selected from C
1～C
14straight or branched alkyl or alkyl derivative, R
8be selected from C
1～C
18straight or branched alkyl or alkyl derivative.
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| FR2920782B1 (en) * | 2007-09-07 | 2010-07-30 | Arkema France | DRILLING FLUID CONTAINING CARBON NANOTUBES |
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