CN108485630A - A kind of fluoride silicon surfactant and oil-based foam oil displacement agent containing single perfluoro capryl - Google Patents
A kind of fluoride silicon surfactant and oil-based foam oil displacement agent containing single perfluoro capryl Download PDFInfo
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- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/02—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
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Abstract
Present description provides a kind of fluoride silicon surfactant containing single perfluoro capryl and oil-based foam oil displacement agents.The fluoride silicon surfactant containing single perfluoro capryl has following structure：More ethyoxyls of perfluoro capryl, two short-chain alkyls and specific aggregation degree there are one connecting on silicon atom；It is connected with naphthalene sulfonic acids base by ehter bond in the other end of more ethyoxyls.It is excellent that test shows that the fluoride silicon surfactant with the structure shows in terms of foam stability energy, especially using oil as in the lotion of continuous phase.Meanwhile the surfactant also has good foam performance.Therefore, good foaming and foam stabilizing characteristic base foam flooding finish can be prepared while had using the fluoride silicon surfactant (for gas release up to 300% or more, half foam life period is more than 72h).
Description
Technical field
This specification is related to a kind of fluoride silicon surfactant containing single perfluoro capryl and oil-based foam oil displacement agent.
Background technology
Aerated fluid is applied to the history that oil field development at home and abroad has more than 40 years, and aerated fluid is in the conventional displacement of reservoir oil, tune
Drive, steam bubble drive, steam bubble handle up, cyclic steam foam flooding, the water pumping gas production of aqueous gas well, sand-flushing, drilling well, tune
It cuts open, water blockoff, acidification, all various aspects in the oil-gas field developments such as well cementing of cement and pressure break are obtained for application, and achieve affirmative
Effect.
Largely practice have shown that, foam flooding is the important means for protecting oil reservoir, preventing oil layer pollution, improving oil and gas production.
As the degree of recognition of foam technology is continuously improved in people, foam flooding means and foam flooding finish will become tertiary oil recovery
One of leading technology.
There are a large amount of hypotonic water-sensitive oil fields in the oil field in China, channel is narrow, oozes in above-mentioned oil field stratum mostly stratum
Saturating rate is extremely low, and oil reservoir is migrated difficulty in the earth formation；And it is mostly the water-sensitive formations such as montmorillonite that stratum, which is constituted, water-swellable will originally
Narrow channel block causes oil extraction operation that can not carry out.Therefore, conventional water drive or water base can not be taken for above-mentioned oil reservoir
Foam flooding.
Oil-based foam drive is the effective means to solve the above problems.Using oily (usually using diesel oil or mineral oil) as continuous phase
Foam flooding finish be referred to as oil-based foam oil displacement agent.Compared with water base foam oil displacement agent, the main spy of oil-based foam oil displacement agent
Point is energy high temperature resistance, has very strong inhibition and salt resistance, resistant to pollution ability, lubricity good, and can be effectively prevented from water drive and make
At the stratum such as montmorillonite expand passage the problem of, mitigate the damage to oil-gas Layer.
But oil phase compares that water its surface energy is extremely low, and formation of foam is difficult, and is not easy to stablize, and therefore, makes in water base oil displacement agent
The requirement to form suitable oil-based foam is not achieved in Traditional blowing agents completely.For this reason, it may be necessary to which technical staff's exploitation is directed to oil base
The suitable oil displacement agent of foam system.Currently, existing oil-based foam oil displacement agent is mainly by oil, water, foaming agent, foam stabilizer, emulsification
The compositions such as agent；System is using water as dispersed phase, and using oil as continuous media, the materials such as addition emulsifier, foaming agent, foam stabilizer are formed
Similar oils property emulsion foam system, also known as inverse emulsification foam flooding finish, grease volume ratio is at (50-80)：
The left and right (50-20).For oil-based foam oil displacement agent, gas release (foaming characteristic) and half foam life period (foam stability) are two most important
Index, technical staff exploring always scheme (the usual gas release of the gas release, half foam life period that how to improve oil displacement agent
300% or more, half-life period is likely to the application value for having certain more than 1h, it is therefore desirable to more than 10h), among these, and with foam
The raising of half-life period is problem most outstanding.For example, the formula of Tian Yunfeng et al. exploitations is：It is added 1.5% in 100ml diesel oil
AE-a and AE-b compounding foaming agent and 0.5% modified ethylene propylene ene-type polymer (PHB)；Test result is aobvious
Show, foam volume has reached 500ml (being equivalent to 500%), half-life period 353s.Heart-to-heart talk et al. exploitation formula be：In 100ml
The foam stabilizer DRI-YW-1 that 0.1% foaming agent DRI-YF-1 and 2% is added in diesel oil is the master of oil-based foam drilling fluid
Want component part；Test result shows that foam volume has reached 500ml, half-life period 630s.
Invention content
This specification is designed to provide a kind of fluoride silicon surfactant with excellent foam stability energy and oil base bubble
Foam oil displacement agent.
In order to achieve the above objectives, present description provides a kind of fluoride silicon surfactants containing single perfluoro capryl, wherein should
The structural formula of fluoride silicon surfactant is as follows：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation.
The fluoride silicon surfactant has foam stability energy very outstanding, especially in oil-based foam system.
In above-mentioned fluoride silicon surfactant, it is preferable that n 10-18.
In above-mentioned fluoride silicon surfactant, it is preferable that R1And R2It is methyl simultaneously；Alternatively, R1And R2It is ethyl simultaneously.
In above-mentioned fluoride silicon surfactant, it is preferable that X+For Na+Or K+。
This specification additionally provides a kind of preparation method of above-mentioned fluoride silicon surfactant, wherein this method includes following
Step：
Perfluorooctane is reacted with dialkyl group chlorosilane, obtains product A；Product A is set to be reacted with ethylene oxide,
Obtain product B；So that product B is reacted with to croceine acid, obtains the fluoride silicon surfactant.
In the above preparation method, it is preferable that using the mole of perfluorooctane as benchmark, the dosage of dialkyl group chlorosilane
It is 1-1.5 times of perfluorooctane.
In the above preparation method, it is preferable that using the mole of perfluorooctane as benchmark, the dosage of ethylene oxide is complete
10-20 times of fluoro-octane.
In the above preparation method, it is preferable that using the mole of perfluorooctane as benchmark, to the dosage of croceine acid
It is 1-1.2 times of perfluorooctane.
In the above preparation method, it is preferable that in the step of preparing product A, reaction temperature is 50-70 DEG C, when reaction
Between be 0.5-4h.
In the above preparation method, it is preferable that in the step of preparing product B, reaction temperature is 150-170 DEG C, reaction
Time is 0.5-4h.
In the above preparation method, it is preferable that make product B with the step of reaction croceine acid in, reaction
Temperature is 80-120 DEG C, reaction time 0.5-4h.
In the above preparation method, it is preferable that in the step of preparing the product B, including ring-opening polymerization and take
Generation reaction, ring-opening polymerization can be acidic environment or alkaline environment.It is further preferred that the pH value of the acidic environment is
1-3.It is highly preferred that the acid used in the acidic environment is the concentrated sulfuric acid.
In the above preparation method, it is preferable that corresponding steps after reaction, terminate in the reaction of corresponding steps
Afterwards, product A and/or product B are not isolated from reaction system, continue to be fed intake into reaction system to carry out subsequent reactions.
Present description provides a kind of oil-based foam oil displacement agents, wherein includes at least one in the oil-based foam oil displacement agent
The fluoride silicon surfactant containing single perfluoro capryl of the following structural formula of kind：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation.
The oil-based foam oil displacement agent shows very excellent half foam life period.After tested, under conventional additive amount, i.e.,
Make not using other auxiliary reagents, the half foam life period of the oil-based foam oil displacement agent has still been more than substantially 1h.
In above-mentioned oil-based foam oil displacement agent, it is preferable that n 10-18.
In above-mentioned oil-based foam oil displacement agent, it is preferable that R1And R2It is methyl simultaneously；Alternatively, R1And R2It is ethyl simultaneously.
In above-mentioned oil-based foam oil displacement agent, it is preferable that X+For Na+Or K+。
In above-mentioned oil-based foam oil displacement agent, it is preferable that weight of the fluoride silicon surfactant in oil-based foam oil displacement agent
Amount degree is 0.1-10%.Further preferably 1-3%.
This specification additionally provides application of the above-mentioned oil-based foam oil displacement agent in mining mineral oil；It is preferably low in exploitation
It oozes, the application in the mineral oil of water-sensitive oil field.
Description of the drawings
Fig. 1 is the infrared of the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-prepared by this specification experimental example 1
Spectrogram；
Fig. 2 is the foam performance test result figure of oil-based foam oil displacement system in this specification test case 1；
Fig. 3 is the foam stability energy test result figure of oil-based foam oil displacement system in this specification test case 1；
Fig. 4 is the microscopic appearance figure of oil-based foam oil displacement system in this specification test case 1.
Specific implementation mode
In order to which the technical characteristic of this specification, purpose and advantageous effect are more clearly understood, now to this specification
Technical solution carry out it is described further below, but should not be understood as to this specification can practical range restriction.
This specification embodiment provides a kind of fluoride silicon surfactant containing single perfluoro capryl, the surfactant
Structural formula is as follows：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation.
In in above structure, n represents the average value of ethoxy repeating units number, value range 6-22.Due to second
Oxygroup part is formed by epoxyethane ring-expansion polymerization, therefore its aggregate number (i.e. ethyoxyl number) has certain point
Cloth range (i.e. n values range), while according to the proportioning of reaction condition and reactant, distribution has certain variation, can be with
For integer or decimal.Specific value can be determined according to this field usual manner.
For the fluoride silicon surfactant with above structure, belong to a kind of multiple copolymer.
The fluoride silicon surfactant containing single perfluoro capryl has special structure：Perfluor is pungent there are one connecting on silicon atom
More ethyoxyls of base, two short-chain alkyls and specific aggregation degree；Pass through ehter bond and naphthalene sulfonic acids base in the other end of more ethyoxyls
It is connected.It is excellent that test shows that the fluoride silicon surfactant with the structure shows in terms of foam stability energy, is being especially company with oil
In the lotion of continuous phase.In a specific test, by 2% fluoride silicon surfactant using oil as in the lotion of continuous phase, in 72h
The foam system can still keep foam volume to be more than 80% afterwards.As it can be seen that half foam life period actually can be also longer than 72h.And it is normal
The foam stabilizer of rule is used it in oil-based foam system, and the half foam life period of system often only has a few minutes, the mesh from 1 hour
Mark is also poor many.As it can be seen that the fluoride silicon surfactant that present embodiment provides has foam stability energy very outstanding.In addition, rising
Bubble experiment shows (water content is in the foam system of 25-50%), under conventional additive amount, the fluorine silicon face of present embodiment offer
Activating agent, expansion ratio can reach 300% or more.It can be seen that the fluoride silicon surfactant has excellent foaminess simultaneously
Energy and foam stability energy, especially its excellent foam stability energy.Therefore, which not only can greatly promote oil
The half-life period of base foam flooding finish is sent out furthermore, it is possible to solve foaming agent and foam stabilizer in conventional oil base foam flooding agent in performance
Wave the problem of often mutually limiting.New solution can be provided for the developing key obstacle of oil-based foam oil displacement agent.
Based on above-mentioned performance, fluoride silicon surfactant that present embodiment provides both can separately as Blowing agent composition with
Other agents coordinates use, and can also be used separately as foam stabilizer component and other agents coordinates；Alternatively, simultaneously as foaming
Agent component and foam stabilizer component are used with other agents coordinates；Alternatively, being used as emulsifier.
In addition, further test shows that the oil base prepared using the fluoride silicon surfactant that present embodiment provides is steeped
Foam system can obtain the foam size significantly less than conventional scheme.Microscope photo shows, the size master of foam in the system
It concentrates (overwhelming majority is in 20-30 microns) in the micron-scale.And in conventional foam system, milli subject to foam size is general
Meter level (i.e. 100 microns or more).The characteristic allow the fluoride silicon surfactant prepare oil-based foam system gap very
Small low-permeability oilfield realizes good migration, is suitable for low-permeability oilfield, this is that common foaming agent is then difficult to.
Moreover, foam size is smaller, it is less susceptible to vanish, this, which is also the fluoride silicon surfactant, has excellent foam stabilizing characteristic
One of the reason of.For example, when carrying out micro- test to foam, foam can keep former under the extruding of coverslip with the long period
Beginning foam pattern, this illustrates that the small size foam is with good stability and foamy body.This is that present embodiment provides
The another aspect advantage of fluoride silicon surfactant.Since the oil-based foam that the prior art is formed is substantially what naked eyes can be differentiated
Quasi- mm size, foamy body is not high, therefore, in micro- sem observation, due to the squeezing action of coverslip, causes foam
All rupture and can not with micro- sem observation, take pictures.In addition oil-based foam is without electric conductivity, it is difficult to electricity consumption sem observation, therefore it is rarely seen
The report of the microphoto of oil-based foam.But, this reflects the low stability difference of oil-based foam intensity in the prior art just
Universal present situation.
Further, in preparing oil-based foam plant process using fluoride silicon surfactant provided by the embodiment, fluorine silicon
Surfactant also presents the characteristics of it easily foams.When the foaming agent of common oil-based foam is blistered using Mechanical Method, stirring
Rotating speed need to reach 3000r/min, that is, require foaming that can must implement at high shear rates, this requirement to equipment is very
Height, most equipment cannot achieve, and the fluoride silicon surfactant generally (is preferably in 800-1500r/min as foaming component
Good foaming 1000r/min) can be realized, the requirement to shear rate is greatly reduced, and is conducive under the rough circumstances such as oil field
Implement.
Present embodiment provide fluoride silicon surfactant in, be preferably n be 10-18.The embodiment is than other
Selection has foaming characteristic more outstanding and foam stability.
In the fluoride silicon surfactant that present embodiment provides, R1And R2Can be methyl simultaneously；Alternatively, R1And R2It can be same
When be ethyl.Both schemes difference in performance is little, it is contemplated that if economy, R1And R2It is simultaneously the scheme of methyl
It is more with practical value.
In the fluoride silicon surfactant that present embodiment provides, X+For balance sulfonic group anionic charge metal sun from
Son.In preferred embodiments, X+For Na+Or K+。
Present embodiments provide for a kind of preparation method of the fluoride silicon surfactant containing single perfluoro capryl, the fluorine silicon faces
The structural formula of activating agent is：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation；Preparation method includes
Following steps：
Perfluorooctane is reacted with dialkyl group chlorosilane, obtains product A；Product A is set to be reacted with ethylene oxide,
Obtain product B；So that product B is reacted with to croceine acid, obtains fluoride silicon surfactant.
In the preparation method that above-mentioned present embodiment provides, product A is a chlorine in dialkyl group chlorosilane by perfluor
Compound after octyl substitution；Product B is the compound after another chlorine in dialkyl group chlorosilane is replaced by polyethoxy.Production
When object B is with croceine acid is reacted, the terminal hydroxy group of polyethoxy can occur and to phenolic hydroxyl group on croceine acid
" etherificate ", to obtain fluoride silicon surfactant.
In the preparation method that present embodiment provides, the Conventional solvents in this field can be used.But for preferred side
Case, since main reaction raw materials perfluorooctane, dialkyl group chlorosilane, ethylene oxide are all liquid, substantially may not be used
Plus solvent.
In the preparation method that present embodiment provides, it can be passed through protective gas (nitrogen etc.) in reaction process, make anti-
There should be preferable yield.In addition, stirring can be usual manner, to mixing speed also without particular/special requirement.
In the preparation method that present embodiment provides, when preparing product A, raw material proportioning can be according to conventional arrangement.By
Then monosubstituted to the progress of dialkyl group chlorosilane, therefore, the dosage (mole) of perfluorooctane is generally less than dialkyl group chlorine silicon
Alkane.In a preferred embodiment, using the mole of perfluorooctane as benchmark, the dosage of dialkyl group chlorosilane is that perfluor is pungent
1-1.5 times of alkane.The reaction condition of the step can also be according to conventional arrangement.In a preferred embodiment, reaction temperature can
Think 50-70 DEG C；Reaction time can be 0.5-4h.In most cases, this step reaction can be completed in 1-2h.In addition, should
Step substitution reaction is easier to carry out, and preferable effect is also can get without using catalyst.Certainly, which is not intended to limit catalysis
The use of agent and other auxiliary reagents.
In the preparation method that present embodiment provides, when preparing product B, it can be set according to the n values of target compound
(step reaction determines that product is a series of mixtures with different length oxyethyl chain to suitable proportioning, at this point, what n referred to
It is the average value of all molecules).In a preferred embodiment, using the mole of perfluorooctane as benchmark, ethylene oxide
Dosage be 10-20 times of perfluorooctane.Step reaction contains the open loop, polymerization and ethyoxyl of ethylene oxide to dioxane
The substitution reaction of the chloro retained in base chlorosilane.The open loop of ethylene oxide can be acidic environment open loop or alkaline environment
Open loop.In a preferred embodiment, using acidic environment open loop.Acidic environment can select conventional inorganic acid to realize,
Such as the concentrated sulfuric acid.The dosage of strong acid, which is subject to, reaches pH value for 1-3 or so.The reaction condition of the step can be according to conventional arrangement.
In a preferred embodiment, reaction temperature can be 150-170 DEG C；Reaction time can be 0.5-4h.Majority of case
Under, this step reaction can be completed in 1-2h.The reaction is not intended to limit the use of other auxiliary reagents.
Present embodiment provide preparation method in, make product B with the step of reaction croceine acid in,
So that the terminal hydroxy group of polyethoxy is carried out " etherificate " with to phenolic hydroxyl group on croceine acid, lives to obtain fluorine silicon face
Property agent.Reaction condition and reactant dosage can be according to conventional arrangements.In a preferred embodiment, reaction temperature 80-
120 DEG C, reaction time 0.5-4h.In a preferred embodiment, using the mole of perfluorooctane as benchmark, to hydroxyl
The dosage of naphthalene sulfonic acids is 1-1.2 times of perfluorooctane.Step reaction is without separately adding special catalyst.Certainly, the reaction is simultaneously
The not use of limiting catalyst and other auxiliary reagents.In addition, if reacted using acidic environment in previous step,
This step " etherificate " after reaction, basification can be carried out, to obtain fluoride silicon surfactant.Alkalizing agent can be with
For reagent commonly used in the art.In a preferred embodiment, basifier is sodium hydroxide, potassium hydroxide.
In the preparation method that present embodiment provides, one kettle way preparation can be used, that is, terminate in the reaction of corresponding steps
Afterwards, product A and/or product B are not isolated from reaction system, continue to be fed intake into reaction system to carry out subsequent reactions.
In one preferred embodiment, this approach includes the following steps：(1) perfluorooctane and dialkyl group chlorosilane is anti-at 50-70 DEG C
Answer 1-2h；(2) after being warming up to 150-170 DEG C after above-mentioned reaction product is acidified with strong acid, ethylene oxide the reaction was continued 1- is added
2h；(3) it is added to croceine acid in above-mentioned reaction product, reacts 1.5-2h；(4) alkalescent is adjusted to sodium hydroxide.
It, generally need not be by the fluoride silicon surfactant of final step preparation in the preparation method that present embodiment provides
It isolates from reaction solution and can be used.But if it is necessary characterization is carried out, it is possible to detach in the following manner
Go out：Make fluoride silicon surfactant at salt after, n-hexane is first added by inorganic salts precipitation (add to without new precipitation generate), and
It is filtered to remove, and then vacuum distillation removes unreacted raw material and solvent at 70 DEG C, then adjusts pH value again and obtain whole production
Object.Certainly, by this kind of fluoride silicon surfactant with different n values it is completely isolated (for individual molecule) be unnecessary
And existing isolation technics it is relatively difficult to achieve.
For above-mentioned fluoride silicon surfactant, those skilled in the art can also be prepared using other suitable modes.But
It is that in comparison, the preparation method flow that this specification provides is short, it is relatively low to reaction environment requirement, and can not use
Expensive catalyst can also realize that one kettle way operates；Therefore, this method has apparent industrial advantages.
Present embodiments provide for a kind of oil-based foam oil displacement agents, wherein includes at least one in the oil-based foam oil displacement agent
The fluoride silicon surfactant containing single perfluoro capryl of the following structural formula of kind：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation.
In the present embodiment, above-mentioned fluoride silicon surfactant is being dispersed phase oil as the emulsification foams of continuous phase using water
System has especially excellent foam stability energy.In specific test, under conventional additive amount, tried even if not using other auxiliary completely
Agent (Traditional blowing agents, foam stabilizer etc.), the foam system can still keep foam volume to be more than 80% after 72h, this is much larger than
The conventional target of 1h half-life period.
In addition, blistering experiment shows in the case where not using other auxiliary reagents completely, water content is 25-50%'s
In foam system, expansion ratio can reach 300% or more.
It can be seen that the oil-based foam oil displacement agent can have good gas release and half-life period, especially half-life period simultaneously
At least up to 72h or more.This means that can not only to solve oil-based foam oil displacement agent half-life period in this field too short for this method
Problem, but also be a kind of gas release and half-life period excellent simultaneously scheme.In the art, gas release and half-life period generally recognize
It is to be difficult to get both, for example, although two prior arts that background technology part is enumerated, the two obtain higher foaming
Amount, but half-life period is too short.In the art, also there is the scheme for attempting balance gas release and half-life period, but result is often the two
It is difficult to meet the requirements simultaneously.For example, in a United States Patent (USP), the scheme for the oil-based foam drilling fluid recorded is：In 100ml
Crude oil in be added 1% foaming agent DC-1250 and 1% foam stabilizer SV-150；Test shows that its half-life period is 4min,
But foam height is also only 180ml (gas release for being equivalent to 180%).
Existing oil-based foam oil displacement agent is often the compounding of various ingredients, and most basic is that foaming agent+foam stabilizer is (most
Emulsifier is also used in the case of number).Foaming agent mainly plays foaming effect, and foam stabilizer is mainly to delay vanishing for foam.For
Often there is repugnance in this kind of conventional oil-based foam system, individual foaming agent and foam stabilizer, this is in performance performance
The gas release and half-life period for leading to system are difficult to the main problem to get both.And the scheme that present embodiment provides, special construction
Fluoride silicon surfactant has had both two kinds of performances in same compound, to overcome above-mentioned problem.It may be fluorine silicon face
Specific structure possessed by activating agent has reconciliation effect to frothing function and foam stabilizing function.
There is the spy of good gas release and half-life period simultaneously based on the oil-based foam oil displacement agent that the above embodiment provides
Point, it is further contemplated that its unique advantage in practical applications.Due in conventional oil-based foam oil displacement agent, foaming agent and
There are larger differences in chemical constitution, functional group and polarity for foam stabilizer, and serious chromatography can occur when migrating in the earth formation
Separation, the different location being respectively in stratum so as to cause each component (or constituent content changes very greatly in each layer), is caused
Each component synergistic effect weakens, even loses, and then often results in oil-based foam agent and be unable to reach expected oil displacement efficiency.And this
The oil-based foam oil displacement agent that embodiment provides, since frothing capacity and foam stability energy are integrated in one by fluoride silicon surfactant,
What it was acted on, which plays to be acted on by stratum chromatographic isolation, is influenced, and accordingly, with respect to conventional oil base oil displacement agent, the program exists
Application has special advantage.But the oil-based foam oil displacement agent that present embodiment provides does not repel the work of fluorine silicon face
Property agent and some other conventional auxiliary reagent compounding.Under compound scheme, since fluoride silicon surfactant can still play
The effect of bubble and foam stabilizing, at least can significantly reduce influence of the chromatographic fractionation effect to oil displacement agent overall effect.
In the oil-based foam oil displacement agent that present embodiment provides, n 10-18.The embodiment has more than other selections
Gas release outstanding and half-life period.
In the oil-based foam oil displacement agent that present embodiment provides, R1And R2It is methyl simultaneously；Alternatively, R1And R2It is simultaneously
Ethyl.Both schemes difference in performance is little, it is contemplated that if economy, R1And R2It is had more simultaneously for the scheme of methyl
It is with practical value.
In the oil-based foam oil displacement agent that present embodiment provides, X+For balance sulfonic group anionic charge metal sun from
Son.In preferred embodiments, X+For Na+Or K+。
In the oil-based foam oil displacement agent that present embodiment provides, fluoride silicon surfactant contains oil-based foam oil displacement agent
Amount can be the conventional additive amount of this field.In a preferred embodiment, fluoride silicon surfactant is in oil-based foam oil displacement agent
Weight percent content be 0.1-10%.In another embodiment, fluoride silicon surfactant is in oil-based foam oil displacement agent
Weight percent content is 1-3%.
In above-mentioned oil-based foam oil displacement agent, it is preferable that it is (low that the wax content of the oil-based foam oil displacement agent is less than 2.5%
Wax).
Application of this specification embodiment further provides above-mentioned oil-based foam oil displacement agent in mining mineral oil；Preferably
Exploiting application hypotonic, in the mineral oil of water-sensitive oil field.
Example
Following experimental example can implement the present invention for the people with general technical ability in this field or verification the verifying results provide ginseng
It examines.These examples are not limit the scope of the claims.
Experimental example 1
The dimethylchlorosilane of 40g perfluorooctane and 12g is placed in reactor, nitrogen protection, 60 DEG C of following stirrings are led to
The concentrated sulfuric acid (pH is made to reach 2 or so) is added in system, is warming up to 150 DEG C, is slowly added to 60g ethylene oxide, the reaction was continued by 1.5h
1.5h is cooled to 100 DEG C or so, and 22g is added and reacts 1.5h to croceine acid, and sodium hydroxide is added and adjusts pH value to 9, obtains
Include the liquid of fluoride silicon surfactant (the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl -).
It after tested and calculates, more ethoxy repeating units number average value n are 16.3 in the present embodiment.
IR Characterization
Since the n values in the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of the dimethyl-of preparation are a data area,
Its molecular weight is not single as a result, can form extremely complex tile structure in mass spectrum, can not be analyzed, and therefore, is not suitable for
Mass Spectrometric Identification；Nuclear-magnetism also has similar problems.For this purpose, this experiment uses the usual characteristic manner of this field, i.e. IR Characterization.
Before the more ethyoxyls of the mono- perfluoro capryl silicon-of dimethyl-to above-mentioned experimental example 1-sodium naphthalene sulfonate carries out IR Characterization,
More ethyoxyl-the sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-can be isolated from reaction solution in the following manner：Make fluorine silicon
Surfactant (is added sodium hydroxide and adjusts pH value to 9) at after salt, and n-hexane is first added and (adds to inorganic salts precipitation without new heavy
Form sediment and generate), and be filtered to remove, and then vacuum distillation removes unreacted raw material and solvent at 70 DEG C, then adjusts again
Section pH value obtains the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of final product-dimethyl-.Obtained infrared spectrum is shown in Fig. 1.
It is as follows to the spectrum unscrambling of infrared spectrum (Fig. 1)：
In 2870cm-1There are the flexible vibrations of this C-H for left and right, in 1395cm-1And 1365cm-1There is the bending of methyl to shake,
And 1365cm-1The intensity at peak is larger, thus proves that dialkyl group chlorosilane has been modified in perfluorooctane.In 3500cm-1It is left
The stretching vibration absworption peak of right presence-OH, in 1200cm-1And 1100cm-1There are the characteristic absorption peaks of S=O at place.In 1600cm-1, 1500cm-1And 1450cm-1There are 3 peaks that intensity does not wait, is the skeletal vibration absorption peak of phenyl ring, in 791cm-1, 772cm-1There is the absorption of C-H out-of-plane bending vibrations in place, thus illustrates that naphthalene sulfonic acids base has been modified.Therefore, above-mentioned infrared spectrum can
To prove product that this experimental example synthesizes as the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-.
Experimental example 2
The dimethylchlorosilane of 40g perfluorooctane and 9.4g is placed in reactor, nitrogen protection, 60 DEG C of following stirrings are led to
The concentrated sulfuric acid (pH is made to reach 2 or so) is added in system, is warming up to 150 DEG C, is slowly added to 40g ethylene oxide, the reaction was continued by 1.5h
1.5h is cooled to 100 DEG C or so, and 20g is added and reacts 1.5h to croceine acid, and sodium hydroxide is added and adjusts pH value to 8.5, obtains
To the liquid for including the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-.
It after tested and calculates, more ethoxy repeating units number average value n are 12.1 in the present embodiment.
Experimental example 3
The dimethylchlorosilane of 40g perfluorooctane and 9.4g is placed in reactor, nitrogen protection, 60 DEG C of following stirrings are led to
The concentrated sulfuric acid (pH is made to reach 2 or so) is added in system, is warming up to 150 DEG C, is slowly added to 55g ethylene oxide, the reaction was continued by 1.5h
1.5h is cooled to 100 DEG C or so, and 21g is added and reacts 1.5h to croceine acid, and sodium hydroxide is added and adjusts pH value to 8, obtains
Include the liquid of the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-.
It after tested and calculates, more ethoxy repeating units number average value n are 15.2 in the present embodiment.
Experimental example 4
The dimethylchlorosilane of 40g perfluorooctane and 14g is placed in reactor, nitrogen protection, 60 DEG C of following stirrings are led to
The concentrated sulfuric acid (pH is made to reach 2 or so) is added in system, is warming up to 150 DEG C, is slowly added to 80g ethylene oxide, the reaction was continued by 1.5h
1.5h is cooled to 100 DEG C or so, and 23g is added and reacts 1.5h to croceine acid, and sodium hydroxide is added and adjusts pH value to 9.5, obtains
To the liquid for including the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-.
It after tested and calculates, more ethoxy repeating units number average value n are 17.9 in the present embodiment.
Experimental example 5
The dimethylchlorosilane of 40g perfluorooctane and 11g is placed in reactor, nitrogen protection, 60 DEG C of following stirrings are led to
The concentrated sulfuric acid (pH is made to reach 2 or so) is added in system, is warming up to 150 DEG C, is slowly added to 62g ethylene oxide, the reaction was continued by 1.5h
1.5h is cooled to 100 DEG C or so, and 22g is added and reacts 1.5h to croceine acid, and sodium hydroxide is added and adjusts pH value to 8.5, obtains
To the liquid for including the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-.
It after tested and calculates, more ethoxy repeating units number average value n are 16.7 in the present embodiment.
Experimental example 6
The dimethylchlorosilane of 40g perfluorooctane and 12g is placed in reactor, nitrogen protection, 60 DEG C of following stirrings are led to
The concentrated sulfuric acid (pH is made to reach 2 or so) is added in system, is warming up to 150 DEG C, is slowly added to 70g ethylene oxide, the reaction was continued by 1.5h
1.5h is cooled to 100 DEG C or so, and 22g is added and reacts 1.5h to croceine acid, and sodium hydroxide is added and adjusts pH value to 9, obtains
Include the liquid of the more ethyoxyl-sodium naphthalene sulfonates of the mono- perfluoro capryl silicon-of dimethyl-.
It after tested and calculates, more ethoxy repeating units number average value n are 17.0 in the present embodiment.
Test case 1
The more ethyoxyls of the mono- perfluoro capryl silicon-of dimethyl-prepared by experimental example 1-sodium naphthalene sulfonate prepares the oil-based foam displacement of reservoir oil
System, specially：
Fluoride silicon surfactant is added to the white oil foam system (low content of wax system) of different moisture content, carries out blistering and steady
Steep the test of performance.
Frothing capacity test is as follows：
(1) white oil is compounded with water according to different proportion, specific proportioning is：Oil/water (95/5；90/10；85/15；
80/20；75/25；70/30；65/35；60/40；55/45；50/50) solution of 10 kinds of different oil-water ratios, is obtained.
(2) the above-mentioned solution of 50mL is taken, the mono- perfluoro capryl of dimethyl-made from experimental example 1 is added in above-mentioned solution system
The more ethyoxyls of silicon-- sodium naphthalene sulfonate 1g.
(3) mechanical agitation realizes emulsification and foaming, stir speed (S.S.) 1000r/min, mixing time 5min simultaneously.
(4) foam system of acquisition is poured slowly into graduated cylinder, measures foam height, obtain frothing percentage result.
All of above test carries out at least parallel laboratory test three times, and test result is 3 validity test result average values.
Result is depicted as to the block diagram of water content and expansion ratio, it is specific such as Fig. 2.
From figure 2 it can be seen that when water content is more than (containing being equal to) 25%, you can reach oil-based foam requirement
300% expansion ratio requirement.
Foam stability energy test is as follows：
The foam system that foam performance is completed to above-mentioned test carries out foam stability test, and test result is shown in Fig. 3.From Fig. 3
It can be seen that：After 72h, the foam retention of the oil based system of different moisture content still reaches 85% or more, that is, illustrates its bubble
Foam half-life period is more than 72h (requirement for being far above 1h).Its foam stability energy meets displacement of reservoir oil requirement.
Fig. 4 is the microcosmic picture (foam system that water content is 30%) when above-mentioned foam system amplifies under 100 times, can be with
Find out：
1, for the average-size of foam at 20-30 μm or so (micron order), the size is more general in the oil-based foam system
Foaming agent formed foam size it is much smaller (regular-type foam it is most subject to it is millimetre-sized i.e. be much larger than 100 microns or more), because
This compares the foam that common foaming agent is formed, and above-mentioned foam system can realize good migration in the low-permeability oilfield of gap very little,
Suitable for low-permeability oilfield, and regular-type foam system is difficult to；
2, foam can still keep original foam pattern under the extruding of coverslip, illustrate that foam has good stabilization
Property and foamy body, are conducive to the oil field displacement of reservoir oil.
Claims (10)
1. a kind of fluoride silicon surfactant containing single perfluoro capryl, which is characterized in that the structural formula of the fluoride silicon surfactant is such as
Under：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation.
2. fluoride silicon surfactant according to claim 1, which is characterized in that in structure above, n 10-18；
Preferably, R1And R2It is methyl simultaneously；Alternatively, R1And R2It is ethyl simultaneously；
It is further preferred that X+For Na+Or K+。
3. a kind of preparation method of fluoride silicon surfactant as claimed in claim 1 or 2, which is characterized in that this method include with
Lower step：
Perfluorooctane is reacted with dialkyl group chlorosilane, obtains product A；
So that product A is reacted with ethylene oxide, obtains product B；
So that product B is reacted with to croceine acid, obtains the fluoride silicon surfactant.
4. the preparation method of fluoride silicon surfactant according to claim 3, which is characterized in that with mole of perfluorooctane
It is 1-1.5 times of perfluorooctane that amount, which is used as benchmark, the dosage of dialkyl group chlorosilane,；
Preferably, the dosage of ethylene oxide is 10-20 times of perfluorooctane；
It is further preferred that 1-1.2 times that the dosage of croceine acid is perfluorooctane.
5. preparation method according to claim 3, which is characterized in that in the step of preparing product A, reaction temperature is
50-70 DEG C, reaction time 0.5-4h；
Preferably, in the step of preparing product B, reaction temperature is 150-170 DEG C, reaction time 0.5-4h；
Preferably, make product B with the step of reaction croceine acid in, reaction temperature is 80-120 DEG C, when reaction
Between be 0.5-4h.
6. preparation method according to claim 3, which is characterized in that corresponding steps after reaction, product A and/
Or product B is not isolated from reaction system, continues to be fed intake into reaction system to carry out subsequent reactions.
7. a kind of oil-based foam oil displacement agent, which is characterized in that include at least one following structural formula in the oil-based foam oil displacement agent
The fluoride silicon surfactant containing single perfluoro capryl：
Wherein, R1Selected from methyl or ethyl；R2Selected from methyl or ethyl；N is 6-22；X+For metal cation.
8. oil-based foam oil displacement agent according to claim 7, which is characterized in that in structure above, n 10-18；
Preferably, R1And R2It is methyl simultaneously；Alternatively, R1And R2It is ethyl simultaneously；
It is further preferred that X+For Na+Or K+。
9. oil-based foam oil displacement agent according to claim 7, which is characterized in that the fluoride silicon surfactant is steeped in oil base
The weight percent content of foam oil displacement agent is 0.1-10%；Preferably 1-3%.
10. application of the claim 7-9 any one of them oil-based foam oil displacement agents in mining mineral oil；Preferably exploiting
Application hypotonic, in the mineral oil of water-sensitive oil field.
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| CN112300377A (en) * | 2020-02-12 | 2021-02-02 | 中国石油天然气股份有限公司 | Alkyl-polyethoxy-sodium naphthalene sulfonate foam oil displacement agent and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102372658A (en) * | 2010-08-23 | 2012-03-14 | 中国石油化工股份有限公司 | Fatty alcohol-polyoxyethylene ether benzene sulfonate and preparation method thereof |
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- 2018-05-11 CN CN201810445644.XA patent/CN108485630A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102372658A (en) * | 2010-08-23 | 2012-03-14 | 中国石油化工股份有限公司 | Fatty alcohol-polyoxyethylene ether benzene sulfonate and preparation method thereof |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112300377A (en) * | 2020-02-12 | 2021-02-02 | 中国石油天然气股份有限公司 | Alkyl-polyethoxy-sodium naphthalene sulfonate foam oil displacement agent and preparation method thereof |
| CN112300377B (en) * | 2020-02-12 | 2022-06-03 | 中国石油天然气股份有限公司 | Alkyl-polyethoxy-sodium naphthalene sulfonate foam oil displacement agent and preparation method thereof |
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