Disclosure of Invention
The invention aims to solve the problems in the prior art, and provides a clay stabilizer for oil well fracturing and a preparation method thereof, which are used for preventing hydration expansion and dispersion migration of clay minerals, reducing damage to low-permeability oil layer permeability and having good temperature resistance and salt resistance.
The invention is realized by the following technical scheme:
the preparation method of the clay stabilizer for oil well fracturing comprises the following steps:
And (2) adding the cyclodextrin sodium sulfonate tertiary amine monomer and N, N-dimethylformamide into the reaction flask under the nitrogen atmosphere, uniformly stirring, adding 3-bromopropene, stirring for reaction, cooling to room temperature after the reaction is finished, and concentrating under reduced pressure to obtain the cyclodextrin amphoteric ion monomer.
And (2) adding acrylic acid, cyclodextrin-based zwitterionic monomer, methoxy polyethylene glycol acrylic ester and deionized water into a reaction flask under the nitrogen atmosphere, uniformly stirring, then dropwise adding ammonium persulfate at the speed of 0.8-1.2mL/min, reacting for 1-3h at 75-90 ℃ after the dropwise adding is finished, cooling to 40-50 ℃, adding triethylamine, regulating the pH value to be neutral, and obtaining the clay stabilizer for oil well fracturing.
Further, in the step (1), the molar ratio relationship of the cyclodextrin sodium sulfonate tertiary amine monomer to the 3-bromopropene is 1:2.5-4.
Further, the reaction temperature in the step (1) is 90-110 ℃ and the reaction time is 24-48h.
Further, in the step (2), the molar ratio relationship of the acrylic acid, the cyclodextrin radical zwitterionic monomer, the methoxy polyethylene glycol acrylate and the ammonium persulfate is 1:0.03-0.15:0.25-0.4:0.005-0.012.
Further, the preparation method of the cyclodextrin sodium sulfonate tertiary amine monomer in the step (1) is carried out according to the following steps:
And S1, under the nitrogen atmosphere, adding 1, 3-diaminopropane and tetrahydrofuran into a reaction flask, uniformly stirring, adding 1, 3-propane sultone and sodium hydride, stirring for reaction, extracting ethyl acetate and deionized water after the reaction is finished, concentrating an organic phase, recrystallizing with ethanol, and filtering to obtain a sodium diamido sulfonate monomer.
And S2, adding sodium diamido sulfonate monomer and methanol into a reaction flask under the nitrogen atmosphere, uniformly stirring, adding allyl cyclodextrin, stirring for reaction, cooling to room temperature after the reaction is finished, concentrating under reduced pressure, and washing with deionized water to obtain the cyclodextrin sodium sulfonate tertiary amine monomer.
Further, in the step S1, the molar ratio of the 1, 3-diaminopropane, the 1, 3-propane sultone and the sodium hydride is 1:2.05-2.2:2.3-2.8.
Further, the reaction temperature in the step S1 is 55-70 ℃ and the reaction time is 8-16h.
Further, in the step S2, the molar ratio relationship of the sodium diamido sulfonate monomer and the allyl cyclodextrin is 1:2.02-2.1.
Further, the reaction temperature in the step S2 is 40-55 ℃ and the reaction time is 12-24h.
Compared with the prior art, the invention has the following beneficial effects:
The invention takes 1, 3-diaminopropane, 1, 3-propane sultone, allyl cyclodextrin and 3-bromopropene as raw materials, and obtains cyclodextrin-based zwitterionic monomers through chemical grafting reaction, and then initiates polymerization with acrylic acid and methoxy polyethylene glycol acrylate to obtain the clay stabilizer for oil well fracturing; the clay stabilizer contains quaternary ammonium salt cations, can be inserted between clay crystal layers, neutralizes electronegativity of clay surfaces, can generate stronger chemical adsorption action with the clay particle surfaces than nonionic polar adsorption groups, is easy to associate to form a reticular structure in chain bundles, realizes complete coating action on clay particles through adsorption, and weakens repulsive force among clay particles; the sodium sulfonate hydration group in the structure can be adsorbed on the surface of clay particles to form a compact hydration layer, so that the contact between water molecules and the clay surface is prevented and delayed, and the purpose of preventing hydration expansion is achieved.
The introduction of cyclodextrin side groups in the molecular chain of the clay stabilizer provides a large number of hydroxyl groups with stronger polarity, and the hydroxyl groups can be closely adsorbed on the surface of clay through the action of hydrogen bonds, so that water molecules are prevented from continuously entering the area between clay crystal layers, the clay crystal layers are bridged, and the clay expansion is inhibited; meanwhile, the existence of the hydrophobic cavity of the cyclodextrin provides a natural barrier for preventing water molecules from entering the clay crystal layer, so that the ability of inhibiting the hydration expansion of the clay is enhanced; the clay stabilizer belongs to a polymer macromolecular structure, and long-chain molecules in the structure can be adsorbed to a plurality of crystal layers and clay particles at the same time, so that hydration expansion and osmotic hydration expansion of the clay surface are effectively reduced, dispersion of the clay and migration of particles are inhibited, and low-valence cations in the clay are difficult to replace from the clay particle surface or wash away by other acid flow, oil flow and water flow through ion exchange; the clay stabilizer contains a huge cyclodextrin side chain, increases the steric hindrance effect, has strong salt hydrolysis resistance, and can achieve the effect of stabilizing clay for a long time.
The clay stabilizer has wide sources of raw materials, simple synthesis and preparation processes, no byproducts, safety and environmental protection; the clay stabilizer has the advantages of high anti-swelling rate, the anti-swelling rate reaches more than 99% under the condition of using the concentration of 0.2wt%, and the clay stabilizer prepared by the invention has good anti-swelling performance, and simultaneously has the properties of washing resistance, temperature resistance and salt resistance, and can be used for development of oil and gas fields.
Detailed Description
The following description of the technical solutions in the embodiments of the present invention will be clear and complete, and it is obvious that the described embodiments are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Unless otherwise indicated, all starting materials and reagents used in the present application are commercially available or may be prepared by known methods.
Preparation of allyl cyclodextrin is carried out by referring to China adhesive, 12 th month of 2010, 19 th volume, 12 th period, synthesis and structural characterization of 6-O-allyl-beta-cyclodextrin: dissolving 1.135g of beta-cyclodextrin in 60mL of anhydrous N, N-dimethylformamide and anhydrous dimethyl sulfoxide with the same volume, adding 3.54g of sodium hydroxide while stirring, stirring at room temperature for 1h, naturally cooling to 5-10 ℃, adding 8mL of allyl bromide while stirring, continuing to react for 48h, standing for 2h after the reaction is finished, concentrating under reduced pressure, washing residues with acetone for multiple times, and performing suction filtration and drying to obtain the allyl cyclodextrin.
Polyethylene glycol methyl ether acrylate with CAS number 32171-39-4 and structural formulaThe molecular weight is 1000.
1, 3-Diaminopropane, CAS number 109-76-2.
1, 3-Propane sultone, CAS number 1120-71-4.
3-Bromopropene with CAS number 106-95-6.
Example 1:
(1) 85mmol of 1, 3-diaminopropane and 340mL of tetrahydrofuran are added into a reaction flask under the nitrogen atmosphere, 180.2mmol of 1, 3-propane sultone and 205mmol of sodium hydride are added after uniform stirring, the reaction is carried out for 12 hours at 65 ℃, ethyl acetate and deionized water are used for extraction, an organic phase is concentrated, ethanol is used for recrystallization, and a sodium diamido sulfonate monomer is obtained after filtration.
(2) Under the nitrogen atmosphere, 75mmol of sodium diamido sulfonate monomer and 750mL of methanol are added into a reaction flask, after being stirred uniformly, 154.5mmol of allyl cyclodextrin is added, the mixture is reacted for 16 hours at 45 ℃, cooled to room temperature, concentrated under reduced pressure, and washed by deionized water, so that the cyclodextrin sodium sulfonate tertiary amine monomer is obtained.
(3) Under the nitrogen atmosphere, 60mmol of cyclodextrin sodium sulfonate tertiary amine monomer and 1080mL of N, N-dimethylformamide are added into a reaction flask, after uniform stirring, 210mmol of 3-bromopropene is added, the reaction is carried out at 100 ℃ for 32h, the reaction is cooled to room temperature, and the cyclodextrin zwitterionic monomer is obtained after decompression concentration. The preparation reaction process is as follows:
(4) Under nitrogen atmosphere, 100mmol of acrylic acid, 3mmol of cyclodextrin-based zwitterionic monomer, 35mmol of methoxypolyethylene glycol acrylate and 75mL of deionized water are added into a reaction flask, after uniform stirring, 0.8mmol of ammonium persulfate is added dropwise at the speed of 1mL/min, after the dropwise addition is finished, the reaction is carried out for 2 hours at 80 ℃, the temperature is reduced to 45 ℃, and triethylamine is added to adjust the pH value to be neutral, so that the clay stabilizer for oil well fracturing is obtained.
Example 2:
(1) 150mmol of1, 3-diaminopropane and 300mL of tetrahydrofuran are added into a reaction flask under the nitrogen atmosphere, after being stirred uniformly, 307.5mmol of1, 3-propane sultone and 345mmol of sodium hydride are added, the mixture is reacted for 8 hours at 70 ℃, the mixture is extracted by ethyl acetate and deionized water, an organic phase is concentrated, ethanol is recrystallized, and the mixture is filtered to obtain a sodium diamido sulfonate monomer.
(2) 120Mmol of sodium diamido sulfonate monomer and 960mL of methanol are added into a reaction flask under the nitrogen atmosphere, after being stirred uniformly, 242.4mmol of allyl cyclodextrin is added, the mixture is reacted for 12 hours at 55 ℃, cooled to room temperature, concentrated under reduced pressure and washed by deionized water, and the cyclodextrin sodium sulfonate tertiary amine monomer is obtained.
(3) 96Mmol of cyclodextrin sodium sulfonate tertiary amine monomer and 1440mL of N, N-dimethylformamide are added into a reaction flask under nitrogen atmosphere, after uniform stirring, 240mmol of 3-bromopropene is added, the reaction is carried out at 110 ℃ for 24 hours, the reaction is cooled to room temperature, and the cyclodextrin zwitterionic monomer is obtained after decompression concentration.
(4) 100Mmol of acrylic acid, 6mmol of cyclodextrin-based zwitterionic monomer, 25mmol of methoxypolyethylene glycol acrylate and 60mL of deionized water are added into a reaction flask under the nitrogen atmosphere, after the mixture is stirred uniformly, 0.5mmol of ammonium persulfate is added dropwise at the speed of 0.8mL/min, after the dropwise addition is finished, the mixture is reacted for 1h at 90 ℃, the temperature is reduced to 50 ℃, and triethylamine is added to adjust the pH value to be neutral, so that the clay stabilizer for oil well fracturing is obtained.
Example 3:
(1) Under nitrogen atmosphere, 32mmol of 1, 3-diaminopropane and 160mL of tetrahydrofuran are added into a reaction flask, after stirring uniformly, 70.4mmol of 1, 3-propane sultone and 89.6mmol of sodium hydride are added, the mixture is reacted for 16 hours at 55 ℃, ethyl acetate and deionized water are used for extraction, an organic phase is concentrated, ethanol is recrystallized, and a sodium diamido sulfonate monomer is obtained by filtration.
(2) Under the nitrogen atmosphere, 25mmol of sodium diamido sulfonate monomer and 300mL of methanol are added into a reaction flask, after being stirred uniformly, 52.5mmol of allyl cyclodextrin is added, the mixture is reacted for 24 hours at 40 ℃, cooled to room temperature, concentrated under reduced pressure, and washed by deionized water, so that the cyclodextrin sodium sulfonate tertiary amine monomer is obtained.
(3) Under the nitrogen atmosphere, 18mmol of cyclodextrin sodium sulfonate tertiary amine monomer and 360mL of N, N-dimethylformamide are added into a reaction flask, after uniform stirring, 72mmol of 3-bromopropene is added, the reaction is carried out at 90 ℃ for 48 hours, the reaction is cooled to room temperature, and the cyclodextrin zwitterionic monomer is obtained after decompression concentration.
(4) 100Mmol of acrylic acid, 9mmol of cyclodextrin-based zwitterionic monomer, 40mmol of methoxypolyethylene glycol acrylate and 80mL of deionized water are added into a reaction flask under a nitrogen atmosphere, after uniform stirring, 1.2mmol of ammonium persulfate is dropwise added at a speed of 1.2mL/min, after the dropwise addition is finished, the reaction is carried out for 3 hours at 75 ℃, the temperature is reduced to 40 ℃, and triethylamine is added to adjust the pH to be neutral, so that the clay stabilizer for oil well fracturing is obtained.
Example 4:
(1) 70mmol of 1, 3-diaminopropane and 245mL of tetrahydrofuran are added into a reaction flask under the nitrogen atmosphere, after being stirred uniformly, 147mmol of 1, 3-propane sultone and 175mmol of sodium hydride are added, the mixture is reacted for 15 hours at 65 ℃, the mixture is extracted by ethyl acetate and deionized water, an organic phase is concentrated, ethanol is recrystallized, and the mixture is filtered to obtain a sodium diamido sulfonate monomer.
(2) Under the nitrogen atmosphere, 65mmol of sodium diamido sulfonate monomer and 685mL of methanol are added into a reaction flask, after being stirred uniformly, 135mmol of allyl cyclodextrin is added, the mixture is reacted for 18 hours at 45 ℃, cooled to room temperature, concentrated under reduced pressure and washed by deionized water, and the cyclodextrin sodium sulfonate tertiary amine monomer is obtained.
(3) 50Mmol of cyclodextrin sodium sulfonate tertiary amine monomer and 900mL of N, N-dimethylformamide are added into a reaction flask under the nitrogen atmosphere, after uniform stirring, 175mmol of 3-bromopropene is added, the reaction is carried out for 32 hours at 105 ℃, the reaction flask is cooled to room temperature, and the cyclodextrin zwitterionic monomer is obtained after decompression concentration.
(4) 100Mmol of acrylic acid, 12mmol of cyclodextrin-based zwitterionic monomer, 30mmol of methoxypolyethylene glycol acrylate and 75mL of deionized water are added into a reaction flask under a nitrogen atmosphere, after uniform stirring, 0.8mmol of ammonium persulfate is added dropwise at a speed of 0.9mL/min, after the dropwise addition is finished, the reaction is carried out for 3 hours at 85 ℃, the temperature is reduced to 50 ℃, and triethylamine is added to adjust the pH value to be neutral, so that the clay stabilizer for oil well fracturing is obtained.
Example 5:
(1) 48mmol of 1, 3-diaminopropane and 168mL of tetrahydrofuran are added into a reaction flask under the nitrogen atmosphere, after being stirred uniformly, 103.2mmol of 1, 3-propane sultone and 120mmol of sodium hydride are added, the mixture is reacted for 10 hours at 65 ℃, the mixture is extracted by ethyl acetate and deionized water, an organic phase is concentrated, ethanol is recrystallized, and the mixture is filtered to obtain a sodium diamido sulfonate monomer.
(2) Under the nitrogen atmosphere, 35mmol of sodium diamido sulfonate monomer and 310mL of methanol are added into a reaction flask, after being stirred uniformly, 72.8mmol of allyl cyclodextrin is added, the mixture is reacted for 24 hours at 50 ℃, cooled to room temperature, concentrated under reduced pressure and washed by deionized water, and the cyclodextrin sodium sulfonate tertiary amine monomer is obtained.
(3) Under the nitrogen atmosphere, 30mmol of cyclodextrin sodium sulfonate tertiary amine monomer and 550mL of N, N-dimethylformamide are added into a reaction flask, after uniform stirring, 108mmol of 3-bromopropene is added, the reaction is carried out at 110 ℃ for 48 hours, the reaction is cooled to room temperature, and the cyclodextrin zwitterionic monomer is obtained after decompression concentration.
(4) Under nitrogen atmosphere, adding 100mmol of acrylic acid, 15mmol of cyclodextrin-based zwitterionic monomer, 35mmol of methoxypolyethylene glycol acrylate and 75mL of deionized water into a reaction flask, uniformly stirring, dropwise adding 1mmol of ammonium persulfate at a speed of 1.1mL/min, reacting at 90 ℃ for 3h after the dropwise addition is finished, cooling to 45 ℃, adding triethylamine, and regulating the pH to be neutral to obtain the clay stabilizer for oil well fracturing.
Comparative example 1
100Mmol of acrylic acid, 3mmol of allyl cyclodextrin, 35mmol of methoxypolyethylene glycol acrylate and 75mL of deionized water are added into a reaction flask under a nitrogen atmosphere, after uniform stirring, 0.8mmol of ammonium persulfate is added dropwise at a speed of 1mL/min, after the dropwise addition is finished, the reaction is carried out for 2 hours at 80 ℃, the temperature is reduced to 45 ℃, and triethylamine is added to adjust the pH to be neutral, so that the clay stabilizer for oil well fracturing is obtained.
Comparative example 2
Into a reaction flask were charged 100mmol of acrylic acid, 3mmol of dimethyldiallylammonium chloride (structural formulaCAS number 7398-69-8), 3mmol of sodium 4-vinylbenzenesulfonate (structural formula2695-37-6) Of CAS number, 35mmol of methoxypolyethylene glycol acrylate and 75mL of deionized water, dropwise adding 0.8mmol of ammonium persulfate at a speed of 1mL/min after uniformly stirring, reacting at 80 ℃ for 2 hours after the dropwise adding is finished, cooling to 45 ℃, adding triethylamine to adjust the pH to be neutral, and obtaining the clay stabilizer for oil well fracturing.
Static clay anti-swelling performance test: the anti-swelling rate of the clay stabilizer is tested by referring to a centrifugation method in SY/T5971-2016 method for evaluating the performance of clay stabilizer for oil and gas field fracturing acidification and water injection. Weighing 0.2g of clay stabilizer prepared in the examples and the comparative examples, adding 100mL of distilled water, and shaking uniformly to obtain clay stabilizer solution; weighing 0.50g of sodium bentonite, loading into a 10mL centrifuge tube, adding 10mL of clay stabilizer solution, shaking fully, standing for 2h at room temperature, loading into a centrifuge, centrifuging at a rotating speed of 1500r/min for 15min, reading the volume V 1 of the sodium bentonite after expansion, respectively replacing the clay stabilizer solution with 10mL of distilled water and kerosene, and measuring the expansion volumes V 2 and V 1 of the bentonite in water and kerosene; the calculation formula of the anti-swelling rate is as follows: b= (V 2-V1)/(V2-V0) ×100%. Wherein B: anti-swelling rate (%); v 0: swelling volume (mL) of bentonite in kerosene; v 1: swelling volume (mL) of bentonite in clay stabilizer; v 2: swelling volume (mL) of bentonite in distilled water.
Table 1 static anti-swelling Performance test
As shown by the test results of the table, with the increase of the content of cyclodextrin-based zwitterionic monomers, the static anti-swelling rate of the clay stabilizer is gradually increased, and the example 5 reaches 99.6%, because on one hand, the clay stabilizer contains quaternary ammonium salt cations inserted between clay crystal layers, and neutralizes electronegativity of the clay surface, so that stronger chemical adsorption effect can be generated with the clay particle surface than nonionic polar adsorption groups, association is easy to generate to form a network structure in chain bundles, complete coating effect on clay particles is realized through adsorption, and repulsive force among clay particles is weakened; the sodium sulfonate hydration groups in the structure can be adsorbed on the surface of clay particles to form a compact hydration layer, so that water molecules are prevented and delayed from contacting the surface of clay, and the purpose of preventing hydration expansion is achieved; on the other hand, the introduction of the cyclodextrin side group in the clay stabilizer provides a large number of hydroxyl groups with stronger polarity, and the hydroxyl groups can be closely adsorbed on the surface of the clay through the action of hydrogen bonds, so that water molecules are prevented from continuously entering the area between the clay crystal layers, the clay crystal layers are bridged, and the clay expansion is inhibited; meanwhile, the existence of the hydrophobic cavity of the cyclodextrin provides a natural barrier for preventing water molecules from entering the clay crystal layer, and enhances the capability of inhibiting the hydration expansion of the clay. The comparative example 1 contains no zwitterionic and the comparative example 2 contains no cyclodextrin, and the rate of expansion is lower than that of the examples.
Washing resistance test: the water-washing resistance of the clay stabilizer was measured by referring to the method specified in SY/T5971-2016 method for evaluating the properties of clay stabilizers for oil and gas field fracture acidizing and water injection. Weighing 0.2g of the clay stabilizer prepared in the examples and the comparative examples, adding 100mL of distilled water, shaking uniformly to obtain a clay stabilizer solution, mixing and centrifuging with 0.50g of bentonite, recording an expansion volume V 1, removing supernatant, adding 10mL of distilled water, shaking uniformly sufficiently, standing for 2h, loading into a centrifuge, centrifuging at 1500r/min for 15min, recording an expansion volume V 2, repeating the steps for 3-8 times, reading the volume after each expansion of bentonite, and judging the washing resistance of the clay stabilizer according to the change condition of the anti-expansion rate.
Table 2 wash resistance test
As shown by the test results of the table, the clay stabilizer solution prepared by the invention has good initial anti-swelling rate, and the anti-swelling rate is over 85 percent after 8 times of water washing and is kept at a higher level, because the clay stabilizer belongs to a polymer macromolecular structure, long-chain molecules in the structure can be adsorbed on a plurality of crystal layers and clay particles at the same time, thereby effectively reducing hydration swelling and osmotic hydration swelling of the clay surface, inhibiting the dispersion of the clay and the migration of particles, so that low-valence cations in the clay are difficult to replace the clay from the clay particle surface or wash the clay particles by other acid flow, oil flow and water flow through ion exchange; therefore, the clay stabilizer prepared by the invention has both economic and scouring-resistant effects, and can achieve the effect of stabilizing clay for a long time.
Temperature resistance test: 0.2g of the clay stabilizer prepared in the examples and the comparative examples is weighed, 100mL of distilled water is added for shaking to obtain a clay stabilizer solution, the clay stabilizer solution is placed in a high-pressure container, the clay stabilizer solution is placed for 30 days at a temperature rising speed of 1 ℃/min to 150 ℃, and a swelling experiment is carried out by using the clay stabilizer after high-temperature treatment according to SY/T5971-2016 'method for evaluating the performance of clay stabilizers for oil and gas field fracturing acidification and water injection'.
Salt resistance test: preparing standard saline with a certain mineralization degree according to the mass ratio (NaCl: caCl 2:MgCl2·6H2 O=7:0.6:0.4), adding a clay stabilizer solution with the mass fraction of 2%, and carrying out an expansion test on the clay stabilizer treated by the saline by using a centrifugal method with reference to SY/T5971-2016 (method for evaluating the performance of clay stabilizers for oil and gas field fracturing and water injection).
TABLE 3 test of temperature and salt resistance
As shown by the test results of the table, after the clay stabilizer is subjected to high-temperature and brine treatment, the anti-swelling rate of the clay stabilizer is more than 80%, and as the clay stabilizer contains a huge cyclodextrin side chain agent, the steric hindrance effect is increased, the anti-salt hydrolysis capability is strong, so that the clay stabilizer prepared by the invention has good anti-swelling performance, and has the washing and high-temperature resistance, and can be used for development of oil and gas fields.
The above examples merely represent a few embodiments of the present application, which are described in more detail and are not to be construed as limiting the scope of the claims. It should be noted that it is possible for those skilled in the art to make several variations and modifications without departing from the concept of the present application, all falling within the scope of protection of the present application; the methods used in the present application are conventional methods unless otherwise specified.