CN101148580A - High-temperature high-salt resistant nano emulsion viscosity-reducing agent - Google Patents
High-temperature high-salt resistant nano emulsion viscosity-reducing agent Download PDFInfo
- Publication number
- CN101148580A CN101148580A CNA2007100504770A CN200710050477A CN101148580A CN 101148580 A CN101148580 A CN 101148580A CN A2007100504770 A CNA2007100504770 A CN A2007100504770A CN 200710050477 A CN200710050477 A CN 200710050477A CN 101148580 A CN101148580 A CN 101148580A
- Authority
- CN
- China
- Prior art keywords
- agent
- nanometer
- viscosity
- water
- nano
- 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.)
- Granted
Links
Landscapes
- Colloid Chemistry (AREA)
- Lubricants (AREA)
- Detergent Compositions (AREA)
Abstract
The present invention relates to high temperature salt resistant nanometer emulsifying thinner comprising surfactant, modifying nanometer assistant, sodium hydroxide, promoter and water. The high temperature salt resistant nanometer emulsifying thinner is prepared through mixing OP-10 in 5-7 %, promoter 2-5 % and modifying nanometer assistant 0.5-2 %, through stirring; adding anionic surfactant 30-45 % and peregal 01-3 %; adding NaOH 20-30 % and water 20-40 %, and stirring through continuous stirring at 60-120 rpm for 60-90 min to obtain the nanometer emulsifying thinner product. The nanometer emulsifying thinner has high stability, small homogeneous oil-in-water grains in high permeating capacity, great capacity of lowering interface tension and high oil displacing efficiency. It is applied for production and conveyance of thick oil.
Description
Technical field:
The present invention relates to a kind of field of petroleum exploitation that is used for, the high-temperature high-salt resistant nano emulsion viscosity-reducing agent of viscous oil recovery and conveying.
Background technology:
At present, though the prescription of emulsifying pour depressor is a lot, but still have more problem: 1. extraction liquid sewage disposal difficulty is big; 2. emulsifying pour depressor is all very strong to the selectivity of viscous crude, does not have universality; 3. present, the emulsifying pour depressor that can be used under high temperature and the high salinity reservoir condition is also few, even some bibliographical informations are arranged, but mostly cost is higher.Therefore, cheap salt tolerant, the resistant to elevated temperatures viscosity-depression agent of research is an important development direction of reducing viscosity by emulsifying technology from now on.In view of the saturating rate maturing field of middle and high infiltration of the most of waterflooding of China, it is moisture to have entered height in addition, and the high recovery percent of reserves productive life, a lot of low permeability oil field porositys are little, and rate of permeation is low, and the low-permeability oil water in field is surveyed rate of permeation 50 * 10
-3Um
2Below, the displacement efficiency of water drive is low, and swept volume is little, the water injection pressure height, exploitation is difficulty, needs new oil recovery technique to solve these problems.The displacement of reservoir oil of nanometer liquid is a kind of emerging oil recovery technique, it is to transmit medium with the aqueous solution, in water, form hundreds of small-particle to tens even several nanometers, have very big specific surface area and surface energy, greatly reduce oil water interfacial tension, make that injecting fluid is washing away the process of hole, make crude oil be easy to peel off into little oil droplet, and the driven liquid displacement is come out.On the other hand, the particle of nanometer liquid has temporary transient ponding to little duct, thereby has enlarged swept volume, and the mother oil displacement that does not feed through to is come out to reach the raising recovery ratio, the purpose of step-down augmented injection.Before the exploitation of this viscosity-depression agent, also there is not a kind of suitable emulsifying pour depressor with good viscosity reduction and oil displacement efficiency, so we utilize the more peculiar functions of nano material and in conjunction with the advantage of various tensio-active agents, the synergy of bringing into play them reaches viscosity reduction synergic purpose.
Summary of the invention
The objective of the invention is to: in order to overcome the steam treatment of single use tensio-active agent, the shortcoming that the viscosity reduction amplitude is little, the cycle is short, utilize the consumption of the organic acid reduction tensio-active agent in the crude oil, the adding of alkaline assistant and nano assistant simultaneously, produce synergy with reducing viscosity by emulsifying, reach the effect of obvious raising reducing viscosity by emulsifying, the spy provides a kind of high-temperature high-salt resistant nano emulsion viscosity-reducing agent.
In order to achieve the above object, the present invention adopts the compound system of nonionic, aniorfic surfactant and nano assistant and other auxiliary agent, and in its molecular structure, hydrophilic and oleophilic is partly alternately arranged, and contains side chain.It can form film at water-oil interface, destroys and prevent the formation of water-in-oil emulsion, makes it form water external emulsion, impels crude oil to be easy to flow, and reaches the purpose of viscosity reduction.
Main technical schemes of the present invention is: a kind of high-temperature high-salt resistant nano emulsion viscosity-reducing agent, it is characterized in that: this nanometer emulsified viscosity-depression agent is made up of nonionogenic tenside, aniorfic surfactant, modified Nano auxiliary agent, sodium hydroxide, promotor, water, and the mass percent of each component and partial properties are: nonionogenic tenside is with OP-10 5～7%, paregal O 1～3%; Aniorfic surfactant 30～45% is with alkylaryl sulphonate, alkyl-sulphate, preferably uses Sodium dodecylbenzene sulfonate, xylogen benzene sulfonic acid sodium salt; Modified Nano auxiliary agent 0.5～2% is with loft drier dried active nano assistant ZnO or nanometer CaCO
3, with tensio-active agent silane coupling agent or the OP-10 that the acetone diluted modification is used, volume ratio 20: 1, again with joining acetone tensio-active agent mixed solution pour in the compressor spray tube, build lid, nano assistant ZnO or nanometer CaCO that drying is good
3Pour in the drum and good seal, improve the pressure of compressor, be controlled at about 0.4MPa, with spray gun solvent liquid is sprayed in the drum, constantly stir the processing of spraying, at last that this property is good nano assistant is put into loft drier acetone is vapored away, and it is 70～90 ℃ that loft drier is provided with temperature; Promotor 2～5% is to use alcohol; NaOH 20～30%; Water 20～40%.
The preparation method of high-temperature high-salt resistant nano emulsion viscosity-reducing agent: the nano assistant ZnO or the CaCO that add OP-10 5～7%, promotor alcohol 2～5%, modification at normal temperatures and pressures successively lentamente
30.5～2%, and stir; Add aniorfic surfactant 30～45% and nonionic surface active agent peregal 01～3% then; Add NaOH 20～30% and water 20～40% at last,, promptly make this nanometer emulsified viscosity-depression agent product again with rotating speed continuously stirring 60～90min of 60～120r/min.
The application of high-temperature high-salt resistant nano emulsion viscosity-reducing agent is: in temperature is that in 20～50 ℃ of water nanometer emulsified viscosity-depression agent to be mixed with mass percent be 0.2～0.3% the aqueous solution; Join temperature again and be in 30～90 ℃ the crude oil, the aqueous solution and crude oil usage ratio are 4: 6～3: 7; Be under 30～120r/min condition at the stirrer rotating speed then, stir 5～15min, form low viscous oil-in-water emulsion, thereby be applied in the exploitation and transportation art of viscous crude.
The present invention compared with prior art has following beneficial effect: (1) this high-temperature high-salt resistant nano emulsion viscosity-reducing agent system is heating power stability and isotropic polycomponent dispersion system, deposit can not take place in the process coalescent; (2) add nano assistant and make the oil-in-water particle of generation littler, more even, thereby improved percolation ability, and discrete nanoparticle can change the porous medium wettability of the surface, can further improve the percolation ability of porous medium; (3) behind the adding nano assistant, its subject range is widened, in the viscosity reduction process, can produce a kind of gas owing to viscosity-depression agent, can produce the effect that mixed phase drives, add that nano assistant can reduce interfacial tension significantly, very helpful to improving oil displacement efficiency, this emulsifying pour depressor can be widely used in the exploitation and the transportation art of viscous crude.
Embodiment
Example 1: high-temperature high-salt resistant nano emulsion viscosity-reducing agent and preparation method thereof
(1) modification of nano assistant:
Take by weighing 100g active nano ZnO and after 80 ℃ of down dry oven dry, pour in the plastic tank of 5000ml, build lid, stay a duck eye covering; Get silane coupling agent 0.5ml, use the 10ml acetone diluted then; With joining solvent pour in the compressor spray tube after the cleaning, build lid.Improve the pressure of compressor, be controlled at about 0.4MPa, with spray gun with joining solvent spray in the keg that active nano ZnO is housed, and constantly stir in good time, at last that this property is good active nano ZnO dryly down vapors away acetone at 85 ℃.
(2) indoor sampling prescription of high-temperature high-salt resistant nano emulsion viscosity-reducing agent and step:
A weighs in the balance and gets large beaker M
1Quality and record, take by weighing the 37.5g of sodium lignosulphonate then and put into M
1In.
B takes by weighing peregal 2.5g and puts into large beaker M
1In.
C is at small beaker M
2In add OP-10 6.25g successively, alcohol 3.75g, modified nano-ZnO 1g also stirs with glass stick, pours large beaker M then into
1In.
D takes by weighing small beaker M
3Quality, add NaOH 25g and add entry 25g again and stir till it fully dissolves with glass stick.
E slowly adds large beaker M to the NaOH aqueous solution for preparing
1In, stir at stink cupboard inner edge edged, till presenting the brown jelly.
Example 2: crude oil emulsion preparation and viscosity reducing effect thereof:
Weigh in the balance and get 100g crude oil and put into 500ml large beaker M
3In, add the viscosity-depression agent that 0.24g has prepared therein, add 43ml water at 7: 3 by water oil ratio at last, (about 50 degrees centigrade) stir with glass stick in water bath with thermostatic control, and viscous crude becomes light brown easy flow state.
Its viscosity reducing effect is as shown in the table:
Table 1
| Dosage/%wt | Viscosity/mPa.s | Viscosity break ratio/% | The emulsification situation |
| 0.1 | 120.4 | 98.76 | Be uniformly dispersed |
| 0.2 | 68.7 | 99.19 | Be uniformly dispersed |
| 0.3 | 14.6 | 99.85 | Be uniformly dispersed |
| 0.4 | 23.3 | 99.76 | Be uniformly dispersed |
| 0.5 | 61.2 | 99.37 | Be uniformly dispersed |
The study condition of this experiment is: used crude oil is 50 ℃ of crude oil that following viscosity is 15610mPa.s, used viscosity tester is that Germany produces HAAKE RV-3 type rotational viscosimeter, the experimental water sample is the simulation highly mineralized formation brines, total mineralization is 12000mg/L, wherein calcium magnesium salinity is 620.5mg/L, Cl
-Content is 197.8mg/L, Na
+, K
+Content is 691.8mg/L.The viscosity reduction contrast and experiment all water oil ratio be 7: 3 and in water bath with thermostatic control (about 50 degrees centigrade) measure.
This emulsifying pour depressor viscosity reducing effect is good as can be seen from the table, consumption is few, very economical, and the optimum amount mass percent concentration is 0.3%, and best pH value is about 11.
Claims (3)
1. high-temperature high-salt resistant nano emulsion viscosity-reducing agent, it is characterized in that: this nanometer emulsified viscosity-depression agent is made up of nonionogenic tenside, aniorfic surfactant, modified Nano auxiliary agent, sodium hydroxide, promotor, water, and the mass percent of each component and partial properties are: nonionogenic tenside is with OP-10 5～7%, paregal O 1～3%; Aniorfic surfactant 30～45% is with alkylaryl sulphonate, alkyl-sulphate, preferably uses Sodium dodecylbenzene sulfonate, xylogen benzene sulfonic acid sodium salt; Modified Nano auxiliary agent 0.5～2% is with loft drier dried active nano assistant ZnO or nanometer CaCO
3, with tensio-active agent silane coupling agent or the OP-10 that the acetone diluted modification is used, volume ratio 20: 1, again with joining acetone tensio-active agent mixed solution pour in the compressor spray tube, build lid, nano assistant ZnO or nanometer CaCO that drying is good
3Pour in the drum and good seal, improve the pressure of compressor, be controlled at 0.4MPa, with spray gun solvent liquid is sprayed in the drum, constantly stir the processing of spraying, at last that this property is good nano assistant is put into loft drier acetone is vapored away, and it is 70～90 ℃ that loft drier is provided with temperature; Promotor 2～5% is to use alcohol; NaOH 20～30%; Water 20～40%.
2. according to right 1 described nanometer emulsified viscosity-depression agent, it is characterized in that: the preparation method of this nanometer emulsified viscosity-depression agent is: the nano assistant ZnO or the CaCO that add OP-10 5～7%, promotor alcohol 2～5%, modification at normal temperatures and pressures successively lentamente
30.5～2%, and stir; Add aniorfic surfactant 30～45% and nonionic surface active agent peregal 01～3% then; Add NaOH 20～30% and water 20～40% at last,, promptly make this nanometer emulsified viscosity-depression agent product again with rotating speed continuously stirring 60～90min of 60～120r/min.
3. according to right 1 described nanometer emulsified viscosity-depression agent, it is characterized in that: the application of nanometer emulsified viscosity-depression agent is: in temperature is that in 20～50 ℃ of water nanometer emulsified viscosity-depression agent to be mixed with mass percent be 0.2～0.3% the aqueous solution; Join temperature again and be in 30～90 ℃ the crude oil, the aqueous solution and crude oil usage ratio are 4: 6～3: 7; Be under 30～120r/min condition at the stirrer rotating speed then, stir 5～15min, form low viscous oil-in-water emulsion, thereby be applied in the exploitation and transportation art of viscous crude.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100504770A CN100516164C (en) | 2007-11-09 | 2007-11-09 | High-temperature high-salt resistant nano emulsion viscosity-reducing agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100504770A CN100516164C (en) | 2007-11-09 | 2007-11-09 | High-temperature high-salt resistant nano emulsion viscosity-reducing agent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101148580A true CN101148580A (en) | 2008-03-26 |
| CN100516164C CN100516164C (en) | 2009-07-22 |
Family
ID=39249281
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2007100504770A Expired - Fee Related CN100516164C (en) | 2007-11-09 | 2007-11-09 | High-temperature high-salt resistant nano emulsion viscosity-reducing agent |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100516164C (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103509541A (en) * | 2012-06-19 | 2014-01-15 | 中国石油化工股份有限公司 | Micro-emulsion viscosity reducer for thick oil, and preparation method thereof |
| CN105754572A (en) * | 2016-05-12 | 2016-07-13 | 河南正佳能源环保股份有限公司 | Method for preparing soluble nano oil-displacing agent |
| CN107739600A (en) * | 2017-11-09 | 2018-02-27 | 重庆科技学院 | The method of thick-oil emulsified adhesive-reducing composition and its reducing viscosity by emulsifying |
| CN111019624A (en) * | 2019-12-23 | 2020-04-17 | 郑州洁灵科技有限公司 | Preparation and application of nano microemulsion for oil displacement |
| CN111777317A (en) * | 2020-07-01 | 2020-10-16 | 遵义市菲科环保科技有限公司 | Composition for reducing viscosity of oil sludge sand condensate and preparation method and application thereof |
| CN113072921A (en) * | 2020-01-06 | 2021-07-06 | 中国石油化工股份有限公司 | Viscosity reducer for ultra-thick oil in shaft |
| CN114015427A (en) * | 2021-11-08 | 2022-02-08 | 中海油田服务股份有限公司 | Nano oil displacement agent and preparation method and application thereof |
| CN115726749A (en) * | 2022-10-21 | 2023-03-03 | 新疆敦华绿碳技术股份有限公司 | High-temperature and high-pressure environment CO 2 Method for improving miscible flooding recovery ratio |
-
2007
- 2007-11-09 CN CNB2007100504770A patent/CN100516164C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103509541A (en) * | 2012-06-19 | 2014-01-15 | 中国石油化工股份有限公司 | Micro-emulsion viscosity reducer for thick oil, and preparation method thereof |
| CN105754572A (en) * | 2016-05-12 | 2016-07-13 | 河南正佳能源环保股份有限公司 | Method for preparing soluble nano oil-displacing agent |
| CN107739600A (en) * | 2017-11-09 | 2018-02-27 | 重庆科技学院 | The method of thick-oil emulsified adhesive-reducing composition and its reducing viscosity by emulsifying |
| CN107739600B (en) * | 2017-11-09 | 2021-03-23 | 重庆科技学院 | Thick oil emulsifying and viscosity reducing composition and emulsifying and viscosity reducing method thereof |
| CN111019624A (en) * | 2019-12-23 | 2020-04-17 | 郑州洁灵科技有限公司 | Preparation and application of nano microemulsion for oil displacement |
| CN113072921A (en) * | 2020-01-06 | 2021-07-06 | 中国石油化工股份有限公司 | Viscosity reducer for ultra-thick oil in shaft |
| CN111777317A (en) * | 2020-07-01 | 2020-10-16 | 遵义市菲科环保科技有限公司 | Composition for reducing viscosity of oil sludge sand condensate and preparation method and application thereof |
| CN114015427A (en) * | 2021-11-08 | 2022-02-08 | 中海油田服务股份有限公司 | Nano oil displacement agent and preparation method and application thereof |
| CN115726749A (en) * | 2022-10-21 | 2023-03-03 | 新疆敦华绿碳技术股份有限公司 | High-temperature and high-pressure environment CO 2 Method for improving miscible flooding recovery ratio |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100516164C (en) | 2009-07-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100516164C (en) | High-temperature high-salt resistant nano emulsion viscosity-reducing agent | |
| CN103320110B (en) | Nano composite high-temperature-resistant extraction aid for thickened oil and super-thickened oil recovery and preparation method thereof | |
| CN110173244B (en) | Viscosity-controllable in-situ emulsification and viscosification system and application thereof in water-drive reservoir | |
| WO2021218019A1 (en) | Nano oil displacement agent, preparation method therefor, and application thereof | |
| CN102786919B (en) | Emulsified asphalt profile control agent | |
| CN111608623B (en) | Biological nano preparation applied to oil and gas resource exploitation | |
| WO2021098467A1 (en) | Permeability-enhancing oil displacement system of tight oil reservoir, preparation thereof and application thereof | |
| CN107556993B (en) | High-temperature-resistant high-salt-resistant biological emulsification viscosity reducer and preparation method thereof | |
| CN108531153B (en) | High-temperature-resistant petroleum resin dispersoid blocking agent and preparation method and application thereof | |
| CN101531891B (en) | Multifunctional nano-viscosity reduction profile control agent | |
| CN109401742A (en) | A kind of heat-resistant salt-resistant foam profile system being formulated by highly mineralized formation brines | |
| CN105331348A (en) | Homogeneous-phase microemulsion oil-displacing agent applied to low-permeation oil field and preparation method of homogeneous-phase microemulsion oil-displacing agent | |
| CN109207133A (en) | A kind of emulsifying and viscosity-reducing agent for condensed oil and preparation method | |
| WO2015074588A1 (en) | Zirconium dispersed-particle gel combination flooding system and preparation method thereof | |
| CN116120908B (en) | Preparation method of ultra-thick oil emulsified viscosity-reducing microemulsion | |
| CN102274701B (en) | Surfactant, preparation and application thereof | |
| CN110511734A (en) | The method for preparing Mobyneb slippery water based on MoS2 nanometer sheet | |
| CN104449630A (en) | Surfactant composition for oil recovery and preparation method of surfactant composition | |
| CN105112038A (en) | Thick oil emulsifying viscosity breaker for tracing steam, and preparation method and application method thereof | |
| CN102925205B (en) | The method of rear viscous crude emulsion breaking is driven for alkali | |
| CN104610952A (en) | Fluoro carbonic composite thickened oil viscosity reducer | |
| CN102020982A (en) | Multiple-effect viscosity depressant for exploiting thickened oil | |
| CN110358519A (en) | A kind of preparation method of low residue salt tolerant fracturing fluid | |
| CN108949139A (en) | It is a kind of to stick preparation method and proppant of the formula from thickening proppant | |
| CN111068923B (en) | Micro-emulsion type coal slime flotation collector and preparation method thereof |
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 | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090722 Termination date: 20121109 |