CN101280181B - Surfactant composition and use thereof - Google Patents
Surfactant composition and use thereof Download PDFInfo
- Publication number
- CN101280181B CN101280181B CN2007100390587A CN200710039058A CN101280181B CN 101280181 B CN101280181 B CN 101280181B CN 2007100390587 A CN2007100390587 A CN 2007100390587A CN 200710039058 A CN200710039058 A CN 200710039058A CN 101280181 B CN101280181 B CN 101280181B
- Authority
- CN
- China
- Prior art keywords
- surfactant composition
- oil
- active agent
- alkyl
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Lubricants (AREA)
Abstract
The invention relates to surface active agent combination and the application of the combination, which solve the problems of bad displacement efficiency under the condition of high temperature and high salt, bringing harm to the strata due to the containing of alkali, equipment and channel corrosion and high production cost found in the oil displacement agent which contains surface active agent in the prior art. The surface active agent combination and the application of the combination solves the problem through the technical proposal of the surface active agent combination which contains alkylphenol polyoxyethylene phosphate ester, polymers and water; the surface active agent combination is applicable to the tertiary oil recovery production of the oil field.
Description
Technical field
The present invention relates to a kind of surfactant composition and uses thereof.
Background technology
China's main oilfield is through once with behind the secondary recovery having entered high water-cut stage, crude production rate descends year by year, for improving oil recovery factor, develop remaining reserves to greatest extent, tertiary oil recovery technology is guaranteeing to have brought into play important effect aspect the oilfield stable production high yield.Ternary composite driving (alkali-polymkeric substance-tensio-active agent) technology of wherein using tensio-active agent be owing to still can increase substantially oil displacement efficiency under the situation of low surfactant consumption, so it has become the new technology at economic and technical all very successful raising oil recovery factor.Its dominant mechanism is: after the oil field enters high water-cut stage, surplus oil with discontinuous oil film by trap in the hole of reservoir rocks, two main power that act on the oil droplet are viscaps, if select suitable surfactant system for use, reduce the interfacial tension between profit, make interfacial tension between the oil bearing reservoir profit from the lower or ultralow value (10 of 20～30 milli ox/Mi Jiangzhi
-3～10
-4Milli ox/rice), just can reduce the resistance that the oil droplet distortion was brought when surplus oil was moved, thereby significantly improve oil displacement efficiency.Tensio-active agent improves oil recovery factor and depends mainly on sweep efficiency and the oil displacement efficiency of tensio-active agent in oil reservoir.Promptly
E?r＝Eυ·E?d
In the formula: E r represents recovery ratio, %; E υ represents sweep efficiency, %; E d represents oil displacement efficiency, %.Therefore, improving E r must start with from improving E v and E d.Promoting agent (comprising tensio-active agent and alkali) has effects such as the oil water interfacial tension of reduction, can improve E d (oil displacement efficiency).This effect can be described by combined effect parameter hollow billet number (N):
E?d∝N
N=motivating force/viscous force ∝ μ υ/Y
Ow
In the formula: μ represents to inject phase viscosity; υ represents to inject the phase flow stream velocity; Y
OwInterfacial tension between the expression profit.Practice proves: reduce residual oil saturation effectively, the hollow billet number must be improved 3～4 orders of magnitude.Because oil reservoir injection rate and pressure are limited, it is not enough therefore depending merely on raising μ and υ, but can be with oil water interfacial tension Y
OwReduce by 3 or the higher order of magnitude, thereby improve the hollow billet number greatly and E d (oil displacement efficiency) is significantly improved, this also is the main oil-displacement mechanism of promoting agent.And to improve sweep efficiency, and main way is the mobility that reduces displacing fluid, this point can realize by adding polymkeric substance increase displacing fluid viscosity.Adopt in the operation three, utilization A S P ternary composite driving (tensio-active agent/alkali/polymkeric substance) flooding system, can make the ultra low interfacial tension between profit that the displacement of reservoir oil (E d) rate of imitating is increased by adding tensio-active agent, (E v) injects alkali to reduce the absorption of tensio-active agent to increase injection fluid viscosity raising sweep efficiency by injection of polymer.Make full use of the useful synergistic combination effect of A S P, improve oil recovery factor (E r).
At present, in tertiary oil recovery, the tensio-active agent that generally uses contains the tensio-active agent of phenyl ring as sulfonated petro-leum, alkylbenzene sulfonate or other.Document CN1458219A discloses the pure binary ultra low interfacial tension of the surfactant polymer combination flooding prescription that a kind of tertiary oil recovery is used, use therein tensio-active agent is sulfonated petro-leum or is the complexed surfactant that host adds thinner and other surfactant compound with the sulfonated petro-leum, the weight percent of its component is a sulfonated petro-leum 50～100%, alkylsulfonate 0～50%, carboxylate salt 0～50%, alkylaryl sulphonate 0～35%, low-carbon alcohol 0～20%.These tensio-active agents have the source extensively, and no matter quantity advantage big, that price is low for common oil reservoir, is combination flooding or single surfactant flooding, all has the mass-producing product, are also obtaining ideal effect aspect the raising recovery ratio.But deep day by day along with the oilfield exploitation degree, the oil recovery stratum is more and more darker, and the use temperature of tensio-active agent is more and more higher, the water-mineralizing degree is also more and more higher.The surfactant system of the above successful Application in common oil reservoir (one, two class oil reservoirs), under the high salt of high temperature (formation temperature is greater than 80 ℃) (more than salinity 20000 mg/litre) condition (three class oil reservoirs), because chemical structure malleable, compound system poor stability produce serious chromatographic separation in oil displacement process, cause the oil displacement efficiency variation.In order to reduce oil/water termination tension force to a greater extent, often add the alkali of high density, as sodium hydroxide, yellow soda ash etc.Alkali can generate new tensio-active agent on the spot with the reaction of acidic substance in the crude oil, and adds tensio-active agent and plays synergistic effect.Document CN1439689A discloses a kind of ternary composite oil-displacing system and application thereof of alkali, mixed surfactant and polymer, and the alkali of wherein selecting for use is Na
2CO
3But in use, alkali not only brings huge injury to stratum and oil well etc., and equipment and corrosive pipeline are serious, spends substantial contribution in maintenance, maintenance; And, have to improve greatly the working concentration of polymkeric substance for reaching required viscosity because alkali can seriously reduce the viscosity and the visco-elasticity of polymkeric substance, the oil recovery comprehensive cost is improved.
Summary of the invention
One of technical problem to be solved by this invention is that the composition that contains tensio-active agent in the prior art exists under the high temperature and high salt condition oil displacement efficiency poor, simultaneously owing to contain alkali, injury is brought on stratum and oil well, etching apparatus and pipeline, the problem that production cost is high provides a kind of new surfactant composition.This surfactant composition still can form 10 with crude oil under alkali-free, high temperature and high salt condition
-3～10
-4Milli ox/rice ultra low interfacial tension.Two of technical problem to be solved by this invention provides a kind of purposes of this surfactant composition.This surfactant composition is applied in the tertiary oil recovery, has the advantages that to improve the high temperature and high salt oil deposit recovery ratio.
For one of solving the problems of the technologies described above, the technical solution used in the present invention is as follows: a kind of surfactant composition comprises following component by weight percentage:
1) 0.01～5.0% alkyl phenol sulfonic polyoxyethylene ether phosphate salt;
2) 0.01～3.0% polymkeric substance;
3) water of surplus;
Wherein said polymkeric substance is at least a in polyacrylamide, modified polyacrylamide or the xanthan gum; The alkyl phenol sulfonic polyoxyethylene ether phosphate salt general molecular formula is:
Wherein M is basic metal, ammonium or amido; R is C
1～C
22Alkyl; N is any one integer in 1～20.
In the technique scheme, the basic metal preferred version is sodium or potassium, and more preferably scheme is a sodium; The R preferred version is C
4～C
15Alkyl, more preferably scheme is C
8～C
12Alkyl; The n preferred version is any one integer in 4～15, and more preferably scheme is any one integer in 5～10.The water preferred version is that clear water or sewage are injected in the oil field.By weight percentage, the consumption preferable range of alkyl phenol sulfonic polyoxyethylene ether phosphate salt is 0.1～1.0%, and more preferably scope is 0.1～0.3%.By weight percentage, the consumption preferable range of polymkeric substance is 0.05～0.5%, and more preferably scope is 0.1～0.2%.
For solve the problems of the technologies described above two, the technical solution used in the present invention is as follows: the application of a kind of surfactant composition in tertiary oil recovery.
The preparation method of alkyl phenol sulfonic polyoxyethylene ether phosphate salt among the present invention may further comprise the steps:
A) alkylphenol and oxyethane are 85～160 ℃ in temperature of reaction, and pressure is under 0～0.40MPa gauge pressure condition, under catalyst action, react alkylphenol polyoxyethylene; The alkyl of wherein said alkylphenol is the alkyl that contains 1～22 carbon atom; The mol ratio of oxyethane and alkylphenol is 1～20: 1; Described catalyzer is the basic cpd of calcium, and consumption is 0.3～3% of an alkylphenol weight;
B) the step a) synthetic alkylphenol polyoxyethylene and the vitriol oil are under 40～60 ℃ of conditions in temperature of reaction, react to get alkyl phenol sulfonic polyoxyethylene ether in 0.5～10 hour; Wherein the mol ratio of the vitriol oil and alkylphenol polyoxyethylene is 2～5: 1;
C) step b) synthetic alkyl phenol sulfonic polyoxyethylene ether and Vanadium Pentoxide in FLAKES are under 60～80 ℃ of conditions in temperature of reaction, reacted 2～6 hours, add entry then 85～90 ℃ of following hydrolysis 1～10 hour, the basic cpd that adds alkali metal containing, ammonium or amido at last, be neutralized to neutrality, get alkyl phenol sulfonic polyoxyethylene ether phosphate salt, wherein the mol ratio of alkyl phenol sulfonic polyoxyethylene ether and Vanadium Pentoxide in FLAKES is 2～3: 1.
Wherein, a) the temperature of reaction preferable range is 140～160 ℃ in the step, and the pressure preferable range is 0.20～0.40MPa gauge pressure; B) the temperature of reaction preferable range is 40～45 ℃ in the step, and the reaction times preferable range is 2～5 hours; C) the temperature of reaction preferable range is 70～75 ℃ in the step, and the reaction times preferable range is 4～5 hours; The alkyl preferred version of described alkylphenol is the alkyl that contains 4～15 carbon atoms, and more preferably scheme is the alkyl that contains 8～12 carbon atoms.The basic cpd preferred version of amino-contained is for being selected from monoethanolamine, diethanolamine or trolamine, and more preferably scheme is for being selected from trolamine.
Alkyl phenol sulfonic polyoxyethylene ether phosphate salt of the present invention can pass through the infrared analysis spectral characterization, and sweep limit is 4000～400cm
-1In wave number is 3100～3000cm
-1, 1609cm
-1, 1512cm
-1, 830cm
-1The place is the absorption characteristic peak of phenyl ring, is 1120cm in wave number
-1The place is the characteristic peak of C-O-C key, is 1350cm in wave number
-1The place is the characteristic peak of polyethylene oxide, at wave number 2840～3000cm
-1The place is the characteristic peak of chain alkyl, is 1251cm in wave number
-1, 680cm
-1The place is for sulfonic characteristic peak on the phenyl ring, at wave number 1250cm
-1The place is the characteristic peak of P=O, 1094cm
-1The place is the charateristic avsorption band of P-O-C.
The tertiary oil recovery that surfactant composition of the present invention is applied to the oil field has the following advantages in producing:
(1) can alkali-free in the composition.The surfactant composition that contains alkyl phenol sulfonic polyoxyethylene ether phosphate salt still can form 10 with underground crude oil under the alkali-free condition
-3～10
-4The ultra low interfacial tension of milli ox/rice has not only overcome when using at the scene high concentration alkali to the huge injury of stratum and oil well, and has met environmental protection requirement, and equipment is not had injury, can reach the oil displacement efficiency of the best;
(2) heatproof, salt tolerant.The surfactant composition that contains alkyl phenol sulfonic polyoxyethylene ether phosphate salt in formation temperature greater than 90 ℃, salinity greater than 60000 mg/litre, Ca
2+, Mg
2+Concentration is still can form 10 with underground crude oil under the condition of 0～2000 mg/litre
-3～10
-4The ultra low interfacial tension of milli ox/rice improves oil recovery factor 16.3%, has obtained better technical effect.
The present invention is further elaborated below by embodiment.
Figure of description
Fig. 1 is the infrared analysis spectrum of alkyl phenol sulfonic polyoxyethylene ether phosphate salt.
Wherein, wave number is 3100～3000cm
-1, 1609cm
-1, 1512cm
-1, 830cm
-1The place is the absorption characteristic peak of phenyl ring, and wave number is 1120cm
-1The place is the characteristic peak of C-O-C key, is 1350cm in wave number
-1The place is the characteristic peak of polyethylene oxide, wave number 2840～3000cm
-1The place is the characteristic peak of chain alkyl, and wave number is 1251cm
-1, 680cm
-1The place is sulfonic characteristic peak on the phenyl ring, wave number 1250cm
-1The place is the characteristic peak of P=O, 1094cm
-1The place is the charateristic avsorption band of P-O-C.
Embodiment
[embodiment 1]
Synthesizing of nonyl phenol sulfonic polyethenoxy (7) ether phosphate sodium
(1) in the reactor that condensing works, whipping appts and gas distributor are housed, adds 110 gram nonyl phenols and 1.2 gram calcium oxide catalysts, when logical nitrogen limit, limit is heated to 135 ℃, add the water of nonyl phenol weight 10%, stirring reaction 1 hour.First then normal pressure steams water, and the back decompression vacuumizes steaming in 20 minutes in 140 ℃ and removes moisture under 20 mmhg vacuum, and this solution is cooled to 80 ℃, slowly drips the vitriol oil of catalyst neutralisation theoretical acid amount 20 weight %.System temperature is heated to 85～90 ℃, open vacuum system, dehydration is 1 hour under high vacuum, then with nitrogen purging 3～4 times with the air in the system of removing, then the system temperature of reaction is transferred to 150 ℃, slowly feed 156 gram oxyethane, control pressure≤0.40MPa carries out alkoxylation; Reaction is used the nitrogen purging system after finishing, and removes unreacted oxyethane, and cooling post neutralization, decolouring, filtration, dehydration get Nonyl pheno (7) ether.
(2) step (1) institute's synthetic nonyl phenol sulfonic polyethenoxy (7) ether is added in the reactor that reflux condensate device, thermometer, agitator are housed be warming up to 45 ℃, stir the vitriol oil that slowly drips 150 grams 98% down, 1.5 add in hour, insulation reaction finished reaction in 2 hours again, got brown viscous liquid through aftertreatment and was alkyl phenol sulfonic polyoxyethylene (7) ether.
(3) step (2) institute synthetic alkyl phenol sulfonic polyoxyethylene ether is placed reactor for 0.5 mole, start whipping appts under≤45 ℃, in 2 hours, 36 gram (0.25 mole) Vanadium Pentoxide in FLAKES powder are added in the reactor, be warming up to 70～75 ℃ then and continue reaction 4 hours, reaction finishes the back and adds 10 gram water, be warming up to 85～90 hydrolysis 2 hours, be cooled to 50 ℃ after hydrolysis is finished and be neutralized to neutrality, get nonyl phenol sulfonic polyethenoxy (7) ether phosphate sodium with aqueous sodium hydroxide solution.
To synthetic nonyl phenol sulfonic polyethenoxy (7) ether phosphate sodium, use U.S. Nicolet-5700 infrared spectrometer, adopt liquid-film method to carry out Infrared spectroscopy (sweep limit 4000～400cm
-1), have characteristic peak shown in Figure 1.
[embodiment 2]
Synthesizing of 4-dodecylphenol sulfonic polyethenoxy (10) ether phosphoric acid triethanolamine salt
(1) adding 130 gram 4-dodecylphenols and 1.3 gram calcium oxide catalysts in the reactor that condensing works, whipping appts and gas distributor are housed when limit logical nitrogen limit heating is made 135 ℃, add the water of 4-dodecylphenol weight 10%, stirring reaction 1 hour.First then normal pressure steams water, and the back decompression vacuumizes steaming in 20 minutes in 140 ℃ and removes moisture under 20 mmhg vacuum, and this solution is cooled to 80 ℃, slowly drips the vitriol oil of catalyst neutralisation theoretical acid amount 20wt%.System temperature is heated to 85～90 ℃, open vacuum system, dehydration is 1 hour under high vacuum, then with nitrogen purging 3～4 times with the air in the system of removing, then the system temperature of reaction is transferred to 150 ℃ and slowly feed 226 gram oxyethane, control pressure≤0.40MPa carries out alkoxylation; Reaction is used the nitrogen purging system after finishing, and removes unreacted oxyethane, and cooling post neutralization, decolouring, filtration, dehydration get dodecyl phenol polyethenoxy (10) ether.
(2) step (1) synthetic 4-dodecylphenol sulfonic polyethenoxy (10) ether is added in the reactor that reflux condensate device, thermometer, agitator are housed be warming up to 45 ℃, stir the vitriol oil that slowly drips 150 grams 98% down, 1.5 add in hour, insulation reaction finished reaction in 2 hours again, got brown viscous liquid through aftertreatment and was alkyl phenol sulfonic polyoxyethylene (10) ether.
(3) step (2) institute synthetic alkyl phenol sulfonic polyoxyethylene ether is placed reactor for 0.5 mole, start whipping appts under≤45 ℃, Vanadium Pentoxide in FLAKES powder with 36 grams (0.25 mole) in 2 hours adds in the reactor, be warming up to 70～75 ℃ then and continue reaction 4 hours, reaction finishes the back and adds 10 gram water, be warming up to 85～90 hydrolysis 2 hours, be cooled to 50 ℃ of trolamine aqueous solution after hydrolysis is finished and be neutralized to neutrality, get 4-dodecylphenol sulfonic polyethenoxy (10) ether phosphoric acid triethanolamine salt with 30 weight %.
To synthetic 4-dodecylphenol sulfonic polyethenoxy (10) ether phosphoric acid triethanolamine salt, use U.S. Nicolet-5700 infrared spectrometer, adopt liquid-film method to carry out Infrared spectroscopy (sweep limit 4000～400cm
-1), have characteristic peak shown in Figure 1.
[embodiment 3]
Synthesizing of octyl phenol sulfonic polyethenoxy (5) ether phosphate ammonium
(1) adding 103 gram 4-dodecylphenols and 1.1 gram calcium oxide catalysts in the reactor that condensing works, whipping appts and gas distributor are housed when limit logical nitrogen limit heating is made 135 ℃, add the water of 4-dodecylphenol weight 10%, stirring reaction 1 hour.First then normal pressure steams water, and the back decompression vacuumizes steaming in 20 minutes in 140 ℃ and removes moisture under 20 mmhg vacuum, and this solution is cooled to 80 ℃, slowly drips the vitriol oil of catalyst neutralisation theoretical acid amount 20 weight %.System temperature is heated to 85～90 ℃, open vacuum system, dehydration is 1 hour under high vacuum, then with nitrogen purging 3～4 times with the air in the system of removing, then the system temperature of reaction is transferred to 150 ℃ and slowly feed 112 gram oxyethane, control pressure≤0.40MPa carries out alkoxylation; Reaction is used the nitrogen purging system after finishing, and removes unreacted oxyethane, and cooling post neutralization, decolouring, filtration, dehydration get octyl phenol polyoxy ethene (5) ether.
(2) step (1) synthetic octyl phenol sulfonic polyethenoxy (5) ether is added in the reactor that reflux condensate device, thermometer, agitator are housed be warming up to 45 ℃, stir the vitriol oil that slowly drips 150 grams 98% down, 1.5 add in hour, insulation reaction finished reaction in 2 hours again, got brown viscous liquid through aftertreatment and was alkyl phenol sulfonic polyoxyethylene (5) ether.
(3) step (2) synthetic alkyl phenol sulfonic polyoxyethylene ether is placed reactor for 0.5 mole, start whipping appts under≤45 ℃, in 2 hours, several times the 36 Vanadium Pentoxide in FLAKES powder that restrain (0.25 mole) are added in the reactor, be warming up to 70～75 ℃ then and continue reaction 4 hours, reaction finishes the back and adds 10 gram water, be warming up to 85～90 hydrolysis 2 hours, be cooled to 50 ℃ of ammonia solns after hydrolysis is finished and be neutralized to neutrality, get octyl phenol sulfonic polyethenoxy (5) ether phosphate ammonia salt with 30%.
To synthetic octyl phenol sulfonic polyethenoxy (5) ether phosphate ammonia salt, use U.S. Nicolet-5700 infrared spectrometer, adopt liquid-film method to carry out Infrared spectroscopy (sweep limit 4000～400cm
-1), have characteristic peak shown in Figure 1.
[embodiment 4]
Get [embodiment 1] synthetic nonyl phenol sulfonic polyethenoxy (7) ether phosphate sodium X (weight) %, polyacrylamide 0.15 (weight) %, Shengli Oil Field win the Tuo Er district and win seven wells injection water, stir 30 minutes, obtain a kind of surfactant composition.Shengli Oil Field wins Tuo Er district victory seven well injection water quality analytical resultss and sees Table 1.In the time of 90.2 ℃, this surfactant composition and Shengli Oil Field win the ultra low interfacial tension that forms between Tuo Er district 0-141 well dewatered oils and see Table 2.Interfacial tension is dripped the interfacial tensimeter measurement with the 500 types rotation that Texas ,Usa university produces.
Table 1
| Project | Cl - | SO 42- | HCO 3 - | Na ++K + | Ca 2+ | Mg 2＝ | Water-mineralizing degree TDS | The water type |
| Mg/litre | 10150 | 0 | 516 | 6231 | 322 | 93 | 27312 | CaCl 2 |
Table 2
| X (weight) % | 0.05 | 0.1 | 0.2 | 0.3 |
| Interfacial tension (milli ox/rice) | 0.0067 | 0.0042 | 0.0028 | 0.00053 |
[embodiment 5]
Get [embodiment 2] synthetic 4-dodecylphenol sulfonic polyethenoxies (10) ether phosphoric acid triethanolamine salt X (weight) %, polyacrylamide 0.15 (weight) %, Shengli Oil Field win Tuo Er district sewage, stir 30 minutes, obtain a kind of surfactant composition.Shengli Oil Field wins Tuo Er district 0-141 well output water Analysis Results of Water Quality and sees Table 3.In the time of 90.2 ℃, this surfactant composition and Shengli Oil Field win the ultra low interfacial tension that forms between Tuo Er district 0-141 well dewatered oils and see Table 4.Interfacial tension is dripped the interfacial tensimeter measurement with the 500 types rotation that Texas ,Usa university produces.
Table 3
| Project | Cl - | SO 4 2- | HCO 3 - | Na ++K + | Ca 2+ | Mg 2＝ | Water-mineralizing degree TDS | The water type |
| Mg/litre | 13535 | 0 | 761 | 8252 | 499 | 126 | 23175 | CaCl 2 |
Table 4
| X (weight) % | 0.05 | 0.1 | 0.2 | 0.3 |
| Interfacial tension (milli ox/rice) | 0.0095 | 0.0078 | 0.0045 | 0.00077 |
[embodiment 6]
Get [embodiment 3] synthetic octyl phenol sulfonic polyethenoxies (5) ether phosphate ammonium X (weight) %, polyacrylamide 0.15 (weight) %, total mineralization is 60000 mg/litre, Ca
2+, Mg
2+Concentration is the preparation water of 2000 mg/litre, stirs 30 minutes, obtains a kind of surfactant composition.In the time of 90.2 ℃, this surfactant composition and Shengli Oil Field win the ultra low interfacial tension that forms between Tuo Er district 0-141 well dewatered oils and see Table 5.Interfacial tension is dripped the interfacial tensimeter measurement with the 500 types rotation that Texas ,Usa university produces.
Table 5
| X (weight) % | 0.05 | 0.1 | 0.2 | 0.3 |
| Interfacial tension (milli ox/rice) | 0.0074 | 0.0069 | 0.0045 | 0.00052 |
[embodiment 7～9]
In length is 30 centimetres, and diameter is 2.5 centimetres, and rate of permeation is 1.5 microns
2Rock core on carry out oil displacement test.Earlier win Tuo Er district local water with Shengli Oil Field and be driven to moisturely 92%, behind the surfactant composition of metaideophone 0.3pv (rock pore volume) [embodiment 4～6], water drive is extremely moisture 100%, can improve oil recovery factor 16.3%.
Claims (9)
1. surfactant composition comprises following component by weight percentage:
1) 0.01～5.0% alkyl phenol sulfonic polyoxyethylene ether phosphate salt;
2) 0.01～3.0% polymkeric substance;
3) water of surplus;
Wherein said polymkeric substance is at least a in polyacrylamide, modified polyacrylamide or the xanthan gum; Described alkyl phenol sulfonic polyoxyethylene ether phosphate salt general molecular formula is:
Wherein M is basic metal, ammonium or amido; R is C
1～C
22Alkyl; N is any one integer in 1～20.
2. surfactant composition according to claim 1 is characterized in that basic metal is sodium or potassium; R is C
4～C
15Alkyl; N is any one integer in 4～15.
3. surfactant composition according to claim 2 is characterized in that described basic metal is sodium; R is C
8～C
12Alkyl; N is any one integer in 5～10.
4. surfactant composition according to claim 1 is characterized in that described water is that clear water or sewage are injected in the oil field.
5. surfactant composition according to claim 1 is characterized in that by weight percentage, and the consumption of alkyl phenol sulfonic polyoxyethylene ether phosphate salt is 0.1～1.0%.
6. surfactant composition according to claim 5 is characterized in that by weight percentage, and the consumption of alkyl phenol sulfonic polyoxyethylene ether phosphate salt is 0.1～0.3%.
7. surfactant composition according to claim 1 is characterized in that by weight percentage, and the consumption of polymkeric substance is 0.05～0.5%.
8. surfactant composition according to claim 7 is characterized in that by weight percentage, and the consumption of polymkeric substance is 0.1～0.2%.
9. the application of the described surfactant composition of claim 1 in tertiary oil recovery.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100390587A CN101280181B (en) | 2007-04-04 | 2007-04-04 | Surfactant composition and use thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100390587A CN101280181B (en) | 2007-04-04 | 2007-04-04 | Surfactant composition and use thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101280181A CN101280181A (en) | 2008-10-08 |
| CN101280181B true CN101280181B (en) | 2011-02-09 |
Family
ID=40012860
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2007100390587A Active CN101280181B (en) | 2007-04-04 | 2007-04-04 | Surfactant composition and use thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101280181B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102277147B (en) * | 2010-06-11 | 2013-09-18 | 中国石油化工股份有限公司 | Oil displacement method for high-temperature high-salt oil reservoir |
| CN104277813B (en) * | 2013-07-09 | 2017-06-20 | 中国石油化工股份有限公司 | Oil extraction in oil field composition and preparation method thereof |
| CN104962269A (en) * | 2015-06-17 | 2015-10-07 | 成都高普石油工程技术有限公司 | Chemical flooding compound for tertiary oil recovery |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4828032A (en) * | 1987-10-15 | 1989-05-09 | Exxon Production Research Company | Oil recovery process using alkyl hydroxyaromatic dianionic surfactants as mobility control agents |
| US5049311A (en) * | 1987-02-20 | 1991-09-17 | Witco Corporation | Alkoxylated alkyl substituted phenol sulfonates compounds and compositions, the preparation thereof and their use in various applications |
| CN1560178A (en) * | 2004-02-25 | 2005-01-05 | 石油大学(华东) | Anti-salt type thicking oil reducing viscosity agent and preparation process thereof |
| CN1583942A (en) * | 2004-06-02 | 2005-02-23 | 刘玉勤 | Fuel thickening chemical producing aid and use thereof |
-
2007
- 2007-04-04 CN CN2007100390587A patent/CN101280181B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5049311A (en) * | 1987-02-20 | 1991-09-17 | Witco Corporation | Alkoxylated alkyl substituted phenol sulfonates compounds and compositions, the preparation thereof and their use in various applications |
| US4828032A (en) * | 1987-10-15 | 1989-05-09 | Exxon Production Research Company | Oil recovery process using alkyl hydroxyaromatic dianionic surfactants as mobility control agents |
| CN1560178A (en) * | 2004-02-25 | 2005-01-05 | 石油大学(华东) | Anti-salt type thicking oil reducing viscosity agent and preparation process thereof |
| CN1583942A (en) * | 2004-06-02 | 2005-02-23 | 刘玉勤 | Fuel thickening chemical producing aid and use thereof |
Non-Patent Citations (1)
| Title |
|---|
| CN 1560178 A,全文. |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101280181A (en) | 2008-10-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101279938B (en) | Alkyl phenol sulfonic polyethenoxy ether sodium monosulfosuccinates and preparation thereof | |
| CN101279937B (en) | Alkyl phenol sulfonic polyoxyethylene ether sulfonate and preparation thereof | |
| CN101279935B (en) | Alkyl phenol sulfonic polyoxyethylene ether carboxylate and preparation thereof | |
| CN101279936B (en) | Alkyl phenol sulfonic polyoxyethylene ether sulfate and preparation thereof | |
| CN101279934B (en) | Aliphatic acid polyethenoxy ether sulphonate and preparation thereof | |
| CN103421480B (en) | Surfactant oil displacement composition and method of making the same | |
| CN102464974B (en) | Composition capable of greatly improving crude oil recovery ratio and preparation method thereof | |
| CN102464598B (en) | Fatty acid amide polyoxylethylene ether benzene sulfonate and preparation method thereof | |
| CN101280179B (en) | Surfactant composition and use thereof | |
| CN102250605B (en) | Surfactant formula system for oil displacement and application thereof in tertiary oil recovery | |
| CN101280180B (en) | Surfactant composition and use thereof | |
| CN103965853A (en) | Combined surfactant and its preparation method | |
| CN111088024A (en) | High-temperature high-salt oil reservoir oil-washing agent, preparation method thereof and carbon dioxide oil displacement method | |
| CN101279984B (en) | Alkyl phenol sulfonic polyoxyethylene ether phosphate salt and preparation thereof | |
| CN104109519A (en) | Betaine-polymer oil displacement composition and preparation method thereof | |
| CN103740357A (en) | Low-tension foaming agent composition and preparation method thereof | |
| CN101280181B (en) | Surfactant composition and use thereof | |
| CN101280182B (en) | Surfactant composition and use thereof | |
| CN103540305B (en) | Surfactant composition for chemical displacement of reservoir oil and preparation method thereof | |
| CN104559985B (en) | The displacement of reservoir oil is applied in poly- table pack object and its tertiary oil recovery | |
| CN104559988A (en) | Betaine surfactant, preparation method and application in strengthened oil production | |
| CN104277808A (en) | Oil-displacement surfactant and preparation method thereof | |
| CN103540306B (en) | Three adopt surfactant composition and preparation method thereof | |
| CN104449633A (en) | Crude oil surfactant and preparation method and application thereof | |
| CN104559989A (en) | Hydrocarbyl amine polyoxyethylene ether polyoxypropylene ether sulfonate type betaine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |