CN102504788A - Foaming agent suitable for oil-field development - Google Patents
Foaming agent suitable for oil-field development Download PDFInfo
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- CN102504788A CN102504788A CN2011103272767A CN201110327276A CN102504788A CN 102504788 A CN102504788 A CN 102504788A CN 2011103272767 A CN2011103272767 A CN 2011103272767A CN 201110327276 A CN201110327276 A CN 201110327276A CN 102504788 A CN102504788 A CN 102504788A
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Abstract
The invention provides a foaming agent suitable for oil-field development. The foaming agent suitable for oil-field development comprises the following components by weight percent: 0.05-1.0% of anionic surfactant, 0.05-1.0% of amphoteric surfactant, 0-1.0% of nonionic surfactant, 0.01-1.0% of foam stabilizer, 0-0.8% of inorganic salt and the balance water. The composition and proportioning of the foaming agent can be adjusted at any time according to the actual situations of different application fields of oil-field development, the foaming agent is convenient in production, has wide applicability and remarkable economic benefit; and the foaming agent has good biodegradability and can not pollute the environment or damage the formation.
Description
Technical field
The present invention relates to the oilfield chemical technology field, particularly a kind of whipping agent that is used for oil field foam profile control, the displacement of reservoir oil, drilling well and water pumping gas production.
Background technology
Since proposing with the thought of foam as mobility control agent first in 1958, domestic and international many research institutions have carried out 40 years of researches to foam technology.Foam is used widely in the displacement of reservoir oil, profile control, pressure break and drilling operation at present.Foam is a kind of dispersion system that gas forms in liquid phase under the whipping agent effect; The major cause that foam has profile control, displacement of reservoir oil effect is the seepage characteristic of foam in porous medium; Be foamy " stifled very much not stifled little, the not stifled oil of water blockoff " effect, cause foam in high and low pervious course, evenly to advance.Simultaneously, foam also has certain washing oil ability, thereby foam has the effect that significantly improves RF.
Foam also is widely used in drilling well and the water pumping gas production, and most of exploitation of oil-gas field is to the middle and later periods, and reservoir pressure descends.Adopting foam drilling is best choice, can improve drilling speed, reduce reservoir damage.And the gas recovery well gas production rate reduces, and problems such as water logging occur.The foaming water discharge gas production is simple owing to technology, less investment, instant effect, do not influence to produce and be widely used.
The key problem in technology that foam is used in oil-field development is the foaming properties of whipping agent, and the public patent major part of in the oil field, using about foam all is confined to single Application Areas at present, can not be applicable to a plurality of Application Areass simultaneously.As 98813947.2 a kind of prescription and method that is used for foam flooding is provided; 91103859.0 disclose a kind of foam system that is used for profile control; 200910016512.6 disclose a kind of pore forming material that is used for the heavy crude reservoir displacement of reservoir oil, 200810045167.4 disclose a kind of whipping agent preparation method of used for oil gas field drilling and extracting etc.This has limited the widespread use of foam in oil-field development to a certain extent.The invention provides a kind of whipping agent that is applicable to foam profile control, the displacement of reservoir oil, drilling well and water pumping gas production, its cost is low, free from environmental pollution, do not damage the stratum, is with a wide range of applications.
Summary of the invention
The object of the present invention is to provide a kind of whipping agent that is applicable to the foam profile control in the oil-field development, the displacement of reservoir oil, drilling well and water pumping gas production.It can adjust the composition and the proportioning of whipping agent according to the actual requirements, makes it be applicable to Application Areass different in the oil-field development.
Technical scheme of the present invention is: this is applicable to the whipping agent of oil-field development; Consist of by mass percentage: aniorfic surfactant content is 0.05~1.0wt%; Amphoteric ionic surfactant content is 0.05~1.0wt%, and non-ionics content is 0~1.0wt%, and suds-stabilizing agent content is 0.01~1.0wt%; Inorganic salt content is 0~0.8wt%, and surplus is a water.
Aniorfic surfactant in the whipping agent of the present invention can be one or more mixing as follows: alkyl-sulphate, alkyl alcohol polyoxyethylene ether sulfate, sulfonated alkylbenzene, sulfonated, sulfonated petro-leum, alkyl carboxylate; Amphoteric ionic surfactant can be one or more mixing as follows: alkyl betaine, sultaine, amino acid pattern; Non-ionics can be one or more mixing as follows: alkyl alcohol Soxylat A 25-7, alkylol amide, alkylol amide Soxylat A 25-7, alkyl polyglycoside, amine oxide type.Utilize the composite effect that can play synergy of anionic, amphoteric ion type and non-ionics, its foaming properties is better than single tensio-active agent, and compound system can reduce Financial cost simultaneously.
Suds-stabilizing agent in the whipping agent of the present invention can be one or more mixing as follows: SEPIGEL 305, Zulkovsky starch, modification guanidine glue, Mierocrystalline cellulose, high fatty alcohol, Triple Pressed Stearic Acid ammonium salt.In whipping agent, add suds-stabilizing agent and help increasing the foam solution film strength, improve foamy stability.Suds-stabilizing agent can also reduce tensio-active agent in use because the loss that reservoir rock absorption causes makes tensio-active agent better bring into play its foaming properties simultaneously.
For increasing the compatibleness and the flexibility of whipping agent and reservoir fluid; Can contain inorganic salt in the whipping agent of the present invention; Inorganic salt can be the inorganic salt that contain in the oilfield sewage, also can be one or more mixing as follows: sodium-chlor, sodium sulfate, sodium hydrogencarbonate, yellow soda ash, Repone K, calcium chloride, magnesium chloride.
The present invention has following beneficial effect: (1) this whipping agent can be adjusted the composition and the proportioning of whipping agent at any time according to the practical situation in different application field in the oil-field development, convenient production, wide adaptability.(2) this whipping agent production cost is low, and its whipability and foam stability are good, and the bubble of formation is even; Consumption is few, remarkable in economical benefits.(3) this whipping agent is free from environmental pollution, does not damage the stratum, has favorable biological degradability, does not contain prohibitive materials.
Description of drawings:
Fig. 1 is a foam injection pressure curve.
Embodiment:
The concrete implementation method of the present invention may further comprise the steps:
Further describe the present invention through following embodiment, it should be understood that these embodiment only are used for illustrative purposes, never constitute any restriction of the present invention.Select for use air-flow method foam survey meter and foam flooding device to estimate foaming volume, froth stability, foam profile control and the oil displacement efficiency of whipping agent, practical implementation is following:
Embodiment 1:
With the foam scanner different whipping agents are carried out whipability and foam stability mensuration, air-flow method foam survey meter feeds nitrogen with the 30mL/min flow velocity under 45 ℃ of constant temperatures, inject 5min.The lather volume that produces when gas injection finishes is as the lathering property of whipping agent, and volume (V) promptly bubbles.Lather volume decays to the used time of a half as the froth stability evaluation index, i.e. half foam life period (t).Foam aggregative index (FCI) can consider simultaneously to bubble volume and two indexs of half foam life period, its calculation relational expression be FCI=3Vt/4.
The foaming properties of different whipping agents is as shown in table 1.Can know by table 1; The foaming volume of different whipping agents all is higher than 160mL; Half foam life period is all above 60min; Its foam aggregative index all is higher than 8000mLmin, shows that different whipping agents all have extraordinary foaming properties, can satisfy the different demands of oil field foam profile control, the displacement of reservoir oil, drilling well and water pumping gas production.
The foaming properties of table 1 whipping agent
Embodiment 2:
The foam profile control of whipping agent and oil displacement efficiency experimental technique are following: (a) choose artificial three layers of heterogeneous body core of 4.5cm * 4.5cm * 30cm, the variation coefficient is 0.72, and rate of permeation is 1100 * 10
-3μ m
2About, porosity is 22~25 %.Be evacuated to-1.0MPa two hours, saturation water is measured the core volume of voids then.Saturated Daqing oil field simulated oil (viscosity 9.5cp) is confirmed oil saturation, and is aging more than 12 hours.(b) water displacing oil is to moisture 98%, and record injection pressure, oil offtake and water production rate are calculated waterflood recovery efficiency factor.(d) during foam flooding, gas is selected nitrogen for use, and gas-liquid is injected simultaneously, and vapour-liquid ratio is 1:1, injects the foaming agent solution to be measured of 0.5 times of core volume of voids (PV).And then follow-up water displacing oil is to moisture 98%, and record injection pressure, oil offtake and water production rate are calculated the foam flooding RF.
The foam injection pressure curve of different whipping agents is as shown in Figure 1 in the heterogeneous body core.Can know by Fig. 1 that the foam flooding stage injection pressure of different whipping agents is apparently higher than the injection pressure in water drive stage, and the pressure in follow-up water drive stage also is higher than the water drive stage.This foam that shows that whipping agent of the present invention produces has extraordinary profile control effect.Experiment numbers is that the foam injection pressure that the whipping agent system of 3# produces is higher than two other, and promptly the effect of 3# whipping agent system profile control is best.
The foam flooding experimental result of different whipping agents is as shown in table 2 in the heterogeneous body core.Can be known that by table 2 the foam flooding RF of different whipping agents all is higher than 36%, experiment numbers is that the foam flooding RF of whipping agent system of 3# is near 40%.The foam that comprehensive analyse shows whipping agent of the present invention produces has extraordinary profile control, oil displacement efficiency.
Table 2 foam flooding experimental result
Experiment numbers | Whipping agent is formed and proportioning | Waterflood recovery efficiency factor (%) | Foam flooding RF (%) | Overall recovery factor (%) |
1# | Terminal olefin sodium sulfonate (containing 14 ~ 16 carbon) 0.2wt%, dodecanamide propyl dimethyl betaine 0.18wt%, partially hydrolyzed polyacrylamide (molecular weight 1,600 ten thousand) 0.1% | 34.6 | 36.8 | 71.4 |
2# | Terminal olefin sodium sulfonate (containing 14 ~ 16 carbon) 0.2 wt%, dodecanamide propyl hydroxy sulfo lycine 0.15 wt%, partially hydrolyzed polyacrylamide (molecular weight 1,600 ten thousand) 0.1% | 35.5 | 38.5 | 74.0 |
3# | Terminal olefin sodium sulfonate (containing 14 ~ 16 carbon) 0.6 wt%; Dodecanamide propyl hydroxy sulfo lycine 0.45wt%, alkyl alcohol Soxylat A 25-7 (containing 2 ~ 3 polyoxyethylene groups, 12 ~ 15 alkyl carbon) 0.3 wt%; Partially hydrolyzed polyacrylamide (molecular weight 1,600 ten thousand) 0.2 wt%, calcium chloride 0.4wt% | 34.5 | 39.2 | 73.7 |
Embodiment 3:
The measurement of whipping agent drainability, under 90 ℃ of simulation gas well oil pipe conditions, the method for stirring with air-flow makes foaming agent solution produce foam, measures drainability within a certain period of time.The drainability of different whipping agents is seen shown in the table 3.Can be known that by table 3 liquid carry over of different whipping agents is all near 150mL, the used time of whipping agent that is numbered 3# is the shortest.This shows that different whipping agents all have drainability preferably, can satisfy the demand of gas well foaming water discharge gas production.
The drainability of table 3 whipping agent
Experiment numbers | Whipping agent is formed and proportioning | Liquid carry over (mL) | Take the liquid time (min) |
1# | Terminal olefin sodium sulfonate (containing 14 ~ 16 carbon) 0.5wt%, dodecanamide propyl dimethyl betaine 0.35wt%, partially hydrolyzed polyacrylamide (molecular weight 1,600 ten thousand) 0.02% | 145.6 | 13.4 |
2# | Terminal olefin sodium sulfonate (containing 14 ~ 16 carbon) 0.5wt%, dodecanamide propyl hydroxy sulfo lycine 0.3wt%, partially hydrolyzed polyacrylamide (molecular weight 1,600 ten thousand) 0.02%, sodium-chlor 0.6% | 146.9 | 12.3 |
3# | Terminal olefin sodium sulfonate (containing 14 ~ 16 carbon) 0.6 wt%; Dodecanamide propyl hydroxy sulfo lycine 0.45wt%, alkyl alcohol Soxylat A 25-7 (containing 2 ~ 3 polyoxyethylene groups, 12 ~ 15 alkyl carbon) 0.3 wt%; Partially hydrolyzed polyacrylamide (molecular weight 1,600 ten thousand) 0.04 wt%, calcium chloride 0.4wt% | 149.4 | 9.5 |
Claims (7)
1. whipping agent that is applicable to oil-field development; Consist of by mass percentage: aniorfic surfactant content 0.05~1.0wt%; Amphoteric ionic surfactant content 0.05~1.0wt%, non-ionics content 0~1.0wt%, suds-stabilizing agent content 0.01~1.0wt%; Inorganic salt content 0~0.8wt%, surplus is a water.
2. the whipping agent that is applicable to oil-field development according to claim 1 is characterized in that: said aniorfic surfactant is one or more the mixing among alkyl-sulphate, alkyl alcohol polyoxyethylene ether sulfate, sulfonated alkylbenzene, sulfonated, sulfonated petro-leum, the alkyl carboxylate.
3. the whipping agent that is applicable to oil-field development according to claim 2 is characterized in that: said amphoteric ionic surfactant is one or more the mixing in alkyl betaine, sultaine, the amino acid pattern.
4. the whipping agent that is applicable to oil-field development according to claim 3 is characterized in that: said non-ionics is one or more the mixing in alkyl alcohol Soxylat A 25-7, alkylol amide, alkylol amide Soxylat A 25-7, alkyl polyglycoside, the amine oxide type.
5. the whipping agent that is applicable to oil-field development according to claim 4 is characterized in that: said suds-stabilizing agent is one or more the mixing in SEPIGEL 305, Zulkovsky starch, modification guanidine glue, Mierocrystalline cellulose, high fatty alcohol, the Triple Pressed Stearic Acid ammonium salt.
6. the whipping agent that is applicable to oil-field development according to claim 5; It is characterized in that: said inorganic salt can be one or more the mixing in sodium-chlor, sodium sulfate, sodium hydrogencarbonate, yellow soda ash, Repone K, calcium chloride, the magnesium chloride, also can be the inorganic salt that contain in the oilfield sewage.
7. the whipping agent that is applicable to oil-field development according to claim 6; It is characterized in that: terminal olefin sodium sulfonate 0.6 wt %; Dodecanamide propyl hydroxy sulfo lycine 0.45 wt %, alkyl alcohol Soxylat A 25-7 0.3 wt %, SEPIGEL 305 0.2 wt %; Calcium chloride 0.4 wt %, water surplus.
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