CN109681171B - Method for discharging liquid and producing gas by adopting solid foam water discharging agent composition - Google Patents

Method for discharging liquid and producing gas by adopting solid foam water discharging agent composition Download PDF

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CN109681171B
CN109681171B CN201710969644.5A CN201710969644A CN109681171B CN 109681171 B CN109681171 B CN 109681171B CN 201710969644 A CN201710969644 A CN 201710969644A CN 109681171 B CN109681171 B CN 109681171B
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gas
foam drainage
solid foam
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CN109681171A (en
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何秀娟
张卫东
裘鋆
马俊伟
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China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
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Sinopec Shanghai Research Institute of Petrochemical Technology
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    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
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    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/584Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
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    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/588Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific polymers

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Abstract

The invention relates to a method for draining liquid and producing gas by adopting a solid foam drainage agent composition. The method mainly solves the problems that the existing high-temperature and high-salinity deep well gas well has excessive liquid loading in the development process, so that the gas well has reduced production and even stops spraying, and the liquid foam drainage agent is difficult to fill. The invention adopts a liquid drainage gas production method, which comprises the following steps: 1) placing the foamed drainage agent composition into an aqueous gas well; 2) contacting the foamed drainage agent composition with a gas and water or oil water mixture in an aqueous gas well sufficient to form a foamed fluid, and then lifting the foamed fluid to the surface; the solid foam drainage agent composition comprises the following components: 1 part of an alkylamine polyether carboxylate; 0.1-50 parts of a long-chain polyether nitrogen-containing compound; 0.2-100 parts of solid filler; the technical scheme of 0-0.5 part of adhesive well solves the problem and can be used in the high-temperature and high-salinity deep well drainage and gas production industry.
Figure DDA0001437211170000011

Description

Method for discharging liquid and producing gas by adopting solid foam water discharging agent composition
Technical Field
The invention relates to a method for draining liquid and producing gas by adopting a solid foam drainage agent composition, in particular to a method for draining liquid and producing gas by adopting a solid foam drainage agent composition for a high-temperature high-salinity deep well.
Background
With the enhancement of the exploitation strength of the gas field, the water output of the gas field becomes a key problem restricting the normal production of the gas well. The foam drainage gas production is a drainage gas production technology which is rapidly developed at home and abroad in recent years, and has the advantages of simple equipment, convenience in construction, low cost, wide applicable well depth range, no influence on normal production of gas wells and the like. Foam drainage is to inject foam drainage agent into a well through an oil pipe or an oil casing ring, and foam with certain stability is generated under the stirring of airflow. The liquid phase of the slipping deposition in the pipe is changed into foam, the relative density of fluid at the lower part in the pipe is changed, and the continuously produced gas phase displacement foam flows out of a shaft, so that the accumulated liquid in the shaft is discharged, and the aim of water drainage and gas production is fulfilled.
The development of foam drainage agent since the sixties of the last century is carried out abroad, and surfactants such as sulfonate, benzene sulfonate, alkylphenol polyoxyethylene and the like are mostly selected. At present, a multi-component compound system is mostly adopted in the foam drainage agent for drainage and gas production, and in order to enhance the stability of single foam, auxiliaries such as alkali, alcohol, polymer, alkanolamide and the like are usually added into a formula to form enhanced foam. US7122509 reports a high temperature foam drainage agent formulation, which adopts a research idea of neutralization of anionic surfactant and amine to improve the temperature resistance of the system. US20120279715 reports a foam fluid for increasing oil yield by recovering gas in a gas well, which is an amido group-containing quaternary ammonium salt surfactant with foam discharging and sterilizing functions, a hydrophobic chain is a hydrophobic segment in substituted naphthalene ring, benzene ring or natural oil ester, and the foam fluid has strong chlorine resistance and condensate oil resistance and good corrosion inhibition performance. However, the molecular structure of the polymer contains amide groups which are sensitive to high temperature, so that the polymer has poor adaptability to gas wells with the temperature of more than 100 ℃. China is a technology for researching foam drainage and gas production from the last 80 years, and a patent CN102212348A discloses a salt-resistant and methanol-resistant foam drainage agent, which comprises the following components in percentage by weight: 20-40% of cocamidopropyl betaine, 45-65% of amine oxide, 5-20% of alpha-olefin sulfonate, 5-15% of triethanolamine, 0.2-2% of fluorocarbon surfactant and 0-5% of methanol, wherein the mineralization resistance can reach 18 ten thousand, but the fluorocarbon surfactant is contained in the agent, so that not only is the cost greatly improved, but also the environmental impact is large.
The foam water discharging agent is mainly a water aqua, has the limitation of a plurality of factors such as transportation, storage and the like, and is troublesome to fill on site. CN 105062453A discloses a solid foam drainage agent for gas fields and a preparation method thereof, wherein raw materials comprise sodium dodecyl sulfate, alkylphenol polyoxyethylene, polyacrylamide, trisodium citrate and thiourea, and the solid foam drainage agent has good foam drainage performance. However, sodium dodecyl sulfate contains a sulfate bond, and the temperature resistance is insufficient.
Disclosure of Invention
The invention aims to solve the technical problems that the gas well is reduced in yield, even stops spraying and is difficult to fill liquid due to excessive liquid loading in the development process of the existing high-temperature high-salinity deep well gas well, and provides a method for draining liquid and producing gas by adopting a solid foam water discharging agent composition, in particular a method for draining liquid and producing gas by adopting the solid foam water discharging agent composition in a high-temperature high-salinity deep well, which is used for draining water and producing gas in the gas well, can carry liquid with high efficiency and has good temperature resistance, salt resistance, foaming performance and liquid carrying capacity.
In order to solve the technical problems, the technical scheme adopted by the invention is as follows: a method for draining liquid and producing gas by using a solid foam drainage agent composition comprises the following steps:
(1) throwing the solid foam drainage agent composition into an aqueous gas well;
(2) contacting the solid foamed drainage agent composition with sufficient gas and water or a gas and oil water mixture in an aqueous gas well to form a foamed fluid, and then lifting the foamed fluid to the surface;
the solid high-temperature-resistant high-salinity foam drainage agent composition for drainage and gas recovery comprises the following components in parts by mass:
(1)1 part of an alkylamine polyether carboxylate;
(2) 0.1-50 parts of a long-chain polyether nitrogen-containing compound;
(3) 0.2-100 parts of solid filler;
(4)0 to 0.5 parts of adhesive.
In the above technical solution, the general molecular formula of the alkylamine polyether carboxylate is preferably:
Figure BDA0001437211150000021
wherein R is1Is C8~C20Any one of the alkyl groups of (a); m, n, p and q are any number of 0-20 independently, and m + n is more than or equal to 1. Further, m + p is preferably any number of 1 to 5, n + q is preferably any number of 5 to 15, and X is at least one of an alkali metal ion and an ammonium ion.
In the above technical solution, the molecular general formula of the long-chain polyether nitrogen-containing compound is preferably:
Figure BDA0001437211150000031
in the formula (II), R1Is C10~C26Fatty radical or C of10~C26An aromatic group of (a); y is 0-20, and z is 0-60; r4、R5Is independently selected from C1~C5Alkyl of (C)1~C5Any one of the substituted alkyl groups of (a); r6、R7Is independently selected from C1~C5Alkylene of (C)1~C5Any one of the substituted alkylene groups of (a); y is selected from anionic groups which render the molecule of formula (II) electrically neutral; further, R1Preferably C10~C20Alkyl or C10~C20Of an alkylbenzene of, R7Preferably C2H4Or C3H6Z is preferably greater than 0.
In the above-mentioned embodiments, Y may be any anionic group which renders the general molecular formula (II) electrically neutral, and for example, Y is preferably, but not limited to, -COO-、-SO3 -、-HPO4 -Is more preferably-COO-、-SO3 -At least one of (1).
In the above technical solution, the solid filler is preferably at least one of inorganic oxysalt, metal halide, organic carboxylic acid and salt thereof, urea, and biuret; further preferably: the solid filler is preferably at least one of carbonate, bicarbonate, sulfate, phosphate, borate, metal halide, formate, acetate, tartaric acid and salt, citric acid and salt, phthalic acid and salt, gallic acid and salt, urea, biuret, and the like; the adhesive is at least one of dextrin, epoxy resin, polyacrylamide, starch, cellulose, polyethylene glycol and the like.
In the above technical solution, the solid filler is preferably at least one of sodium carbonate, sodium bicarbonate, sodium borate, sodium chloride, sodium acetate, tartaric acid, sodium tartrate, citric acid, sodium citrate, potassium phthalate, urea, and biuret.
In the above technical solution, the binder is preferably at least one of polyacrylamide, starch, and polyethylene glycol.
The foam water discharging agent composition of the invention has no special requirement on water during preparation, and can be deionized water or water containing inorganic mineral substances, and the water containing the inorganic mineral substances can be tap water, oil field formation water or oil field injection water.
In the above technical scheme, the preparation method of the solid foam drainage agent composition comprises the following steps:
when the binder is not equal to 0 part, the method for preparing the solid foam drainage agent composition preferably includes the steps of:
(1) uniformly mixing the alkylamine polyether carboxylate, the long-chain polyether nitrogen-containing compound and the solid filler according to the required mass portion to obtain a mixture;
(2) adding water to the adhesive until the adhesive is completely dissolved to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and pressing and forming to obtain the solid foam drainage agent composition;
when the binder is equal to 0 part, the method for preparing the solid foam drainage agent composition preferably includes the steps of:
(1) uniformly mixing the alkylamine polyether carboxylate, the long-chain polyether nitrogen-containing compound and the solid filler according to the required mass portion to obtain a mixture;
(2) and then the mixture is pressed and formed to prepare the solid foam drainage agent composition.
In the technical scheme, the temperature of the gas well is as high as 180 ℃, and the salinity of formation water applicable to the gas well is 0-250000 mg/L.
The foam drainage agent composition prepared by the method has good compatibility, and can also contain other treating agents commonly used in the field, such as surfactants, polymers, alkali and other oil extraction aids.
The thermal decomposition temperature of the alkylamine polyether carboxylate and the long-chain polyether nitrogen-containing compound in the foam water discharging agent composition is 200 ℃, and the thermal decomposition temperature is not hydrolyzed in aqueous solution; and secondly, the composition simultaneously has functional groups with both negative and positive amphiprotics and nonionic fragments, and multiple hydrophilic groups increase the salt resistance on one hand, and increase the amount of bound water and bound water carried by the foaming agent on the other hand, so that the foam liquid carrying amount is increased, and the liquid separation is slowed down, so that the composition can be applied to the high-temperature high-salinity deep well drainage and gas production process at the temperature of 180 ℃.
By adopting the technical scheme of the invention, the foam performance test is carried out on the foam water discharging agent according to SY/T6465-2000 foamer evaluation method for foam water discharging and gas production, the foaming height is more than 140mm, the liquid carrying amount is more than 140mL, the high-temperature aging is carried out for 24h at 180 ℃ in 0-250,000 mg/L salinity saline, the foam foaming height and the water discharging performance change rate are less than 5%, and the foam water discharging agent has good temperature resistance, salt resistance, foaming performance and liquid carrying capacity, and achieves good technical effects.
The invention is further illustrated by the following examples.
Drawings
FIG. 1 shows a liquid carrying amount measuring apparatus (the height of a jacket vessel is 1 m) for simulating measurement of liquid carrying amount of gas produced by liquid discharge.
Detailed Description
In order to better understand the present invention, the following examples are further provided to illustrate the present invention, but the present invention is not limited to the following examples.
[ example 1 ]
(1) 10 g of alkylamine polyether carboxylate, 20 g of long-chain polyether nitrogen-containing compound and sodium sulfate under normal temperature and normal pressure
Mixing 30 g of the mixture evenly to obtain a mixture;
(2)0.1 g of polyacrylamide is added with 1 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and pressing and forming to obtain the solid foam drainage rod FS-1, wherein the component structure of the solid foam drainage rod FS-1 is detailed in Table 1.
[ example 2 ]
(1) Under normal temperature and pressure, 5 g of alkylamine polyether carboxylate, 50 g of long-chain polyether nitrogen-containing compound and sodium sulfate
30 g of sodium carbonate, 10 g of sodium bicarbonate, 30 g of sodium bicarbonate and 30 g of urea are uniformly mixed to obtain a mixture;
(2) 0.5 g of polyethylene glycol is added with 2 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-2, wherein the component structure of the solid foam drainage rod FS-2 is detailed in table 1.
[ example 3 ]
(1) Under normal temperature and pressure, 50 g of alkylamine polyether carboxylate, 10 g of long-chain polyether nitrogen-containing compound and urea
10 g and 1 g of citric acid are uniformly mixed to obtain a mixture;
(2) adding 0.1 g of starch and 2 g of water into the mixture, and stirring the mixture until the starch is completely dissolved to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-3, wherein the component structure of the solid foam drainage rod FS-3 is detailed in table 1.
[ example 4 ]
(1) Under normal temperature and pressure, 20 g of alkylamine polyether carboxylate, 20 g of long-chain polyether nitrogen-containing compound and urea
20 g, 5 g of sodium chloride and 1 g of sodium citrate, and uniformly mixing to obtain a mixture;
(2) 0.01 g of polyacrylamide is added with 0.5 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-4, wherein the component structure of the solid foam drainage rod FS-4 is detailed in Table 1.
[ example 5 ]
(1) Under normal temperature and pressure, 20 g of alkylamine polyether carboxylate, 10 g of long-chain polyether nitrogen-containing compound and hydrogen carbonate
7 g of sodium, 1 g of sodium borate, 2 g of sodium tartrate and 1 g of biuret are uniformly mixed to obtain a mixture;
(2)0.1 g of polyethylene glycol is added with 1.0 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-5, wherein the component structure of the solid foam drainage rod FS-5 is detailed in table 1.
[ example 6 ]
(1) Under normal temperature and pressure, 10 g of alkylamine polyether carboxylate, 30 g of long-chain polyether nitrogen-containing compound and urea
30 g and 1 g of sodium bicarbonate are uniformly mixed to obtain a mixture;
(2) adding 0.1 g of cellulose and 1.0 g of water into the mixture, and stirring the mixture until the cellulose is completely dissolved to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-6, wherein the component structure of the solid foam drainage rod FS-6 is detailed in Table 1.
[ example 7 ]
(1) Under normal temperature and pressure, 1 g of alkylamine polyether carboxylate, 50 g of long-chain polyether nitrogen-containing compound and sodium sulfate
70 g and 30 g of urea are uniformly mixed to obtain a mixture;
(2) 0.2 g of polyethylene glycol is added with 1.5 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-7, wherein the component structure of the solid foam drainage rod FS-7 is detailed in Table 1.
[ example 8 ]
(1) 10 g of alkylamine polyether carboxylate, 20 g of long-chain polyether nitrogen-containing compound and sodium sulfate under normal temperature and normal pressure
Mixing 30 g of the mixture evenly to obtain a mixture;
(2)0.1 g of polyacrylamide is added with 1 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-8, wherein the component structure of the solid foam drainage rod FS-8 is detailed in Table 1.
[ example 9 ]
(1) 10 g of alkylamine polyether carboxylate, 20 g of long-chain polyether nitrogen-containing compound and sodium sulfate under normal temperature and normal pressure
Mixing 30 g of the mixture evenly to obtain a mixture;
(2)0.1 g of polyacrylamide is added with 1 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-9, wherein the component structure of the solid foam drainage rod FS-9 is detailed in table 1.
[ example 10 ]
(1) 10 g of alkylamine polyether carboxylate, 20 g of long-chain polyether nitrogen-containing compound and sodium sulfate under normal temperature and normal pressure
Mixing 30 g of the mixture evenly to obtain a mixture;
(2)0.1 g of polyacrylamide is added with 1 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain the solid foam drainage rod FS-10, wherein the component structure of the solid foam drainage rod FS-10 is detailed in Table 1.
[ example 11 ]
(1) 10 g of alkylamine polyether carboxylate, 20 g of long-chain polyether nitrogen-containing compound and sodium sulfate under normal temperature and normal pressure
Mixing 30 g of the mixture evenly to obtain a mixture;
(2) the above samples were press molded to produce solid foam drainage bars FS-11, the composition of which is detailed in Table 1.
[ example 12 ]
The solid foam drainage agents of examples 1 to 11 were dissolved in simulated aqueous solutions of 100,000, 200,000, and 250,000mg/L mineralization degrees, respectively, at room temperature and pressure to prepare 5000mg/L aqueous solutions.
[ example 13 ]
The height of the foam starting point after the foam drainage agent was measured and the height of the foam after 5 minutes was measured according to SY/T6465-2000 evaluation method for foam drainage and gas blowing agent, and the results are shown in Table 2.
4000mL/min of nitrogen was continuously introduced into the aqueous foam drainage agent solution, and the amount of foam carried over a period of 15 minutes was measured, and the results are shown in Table 2. The liquid carrying amount measuring apparatus used is shown in FIG. 1.
The test was carried out using a pressure-resistant and acid-resistant aging apparatus, and after aging at 180 ℃ for 24 hours, the properties such as the initial foaming height, the foam height after 5 minutes, and the liquid carrying amount after 15 minutes were measured again, and the results are shown in Table 2.
[ COMPARATIVE EXAMPLE 1 ]
(1) Using 30 g of alkylamine polyether carboxylate in [ example 1 ], adding no long-chain polyether nitrogen-containing compound, and uniformly mixing with 30 g of sodium sulfate at normal temperature and normal pressure to obtain a mixture;
(2)0.1 g of polyacrylamide is added with 1 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S1;
(4) 1 g of FS-S1 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance, the results of which are shown in Table 3.
[ COMPARATIVE EXAMPLE 2 ]
(1) Using 55 g of alkylamine polyether carboxylate in example 2, without adding long-chain polyether nitrogen-containing compound, uniformly mixing with 30 g of sodium sulfate, 10 g of sodium carbonate, 30 g of sodium bicarbonate and 30 g of urea at normal temperature and normal pressure to obtain a mixture;
(2) 0.5 g of polyethylene glycol is added with 2 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S2;
(4) 1 g of FS-S2 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance, the results of which are shown in Table 3.
[ COMPARATIVE EXAMPLE 3 ]
(1) Using 60 g of alkylamine polyether carboxylate in [ example 3 ], adding no long-chain polyether nitrogen-containing compound, and uniformly mixing with 10 g of urea and 1 g of citric acid at normal temperature and normal pressure to obtain a mixture;
(2) adding 0.1 g of starch and 2 g of water into the mixture, and stirring the mixture until the starch is completely dissolved to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S3;
(4) 1 g of FS-S3 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance, the results of which are shown in Table 3.
[ COMPARATIVE EXAMPLE 4 ]
(1) Using 40 g of alkylamine polyether carboxylate in [ example 4 ], adding no long-chain polyether nitrogen-containing compound, and uniformly mixing with 20 g of urea, 5 g of sodium chloride and 1 g of sodium citrate at normal temperature and normal pressure to obtain a mixture;
(2) 0.01 g of polyacrylamide is added with 0.5 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S4;
(4) 1 g of FS-S4 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance, the results of which are shown in Table 3.
[ COMPARATIVE EXAMPLE 5 ]
(1) Using 30 g of alkylamine polyether carboxylate in example 5, adding no long-chain polyether nitrogen-containing compound, and uniformly mixing with 7 g of sodium bicarbonate, 1 g of sodium borate, 2 g of sodium tartrate and 1 g of biuret at normal temperature and normal pressure to obtain a mixture;
(2)0.1 g of polyethylene glycol is added with 1.0 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S5;
(4) 1 g of FS-S5 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance, the results of which are shown in Table 3.
[ COMPARATIVE EXAMPLE 6 ]
(1) Using 40 g of alkylamine polyether carboxylate in [ example 6 ], adding no long-chain polyether nitrogen-containing compound, and uniformly mixing with 30 g of urea and 1 g of sodium bicarbonate at normal temperature and normal pressure to obtain a mixture;
(2) adding 0.1 g of cellulose and 1.0 g of water into the mixture, and stirring the mixture until the cellulose is completely dissolved to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S6;
(4) 1 g of FS-S6 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance, the results of which are shown in Table 3.
[ COMPARATIVE EXAMPLE 7 ]
(1) Using 30 g of the long-chain polyether nitrogen-containing compound in example 1, adding no alkylamine polyether carboxylate, and uniformly mixing the long-chain polyether nitrogen-containing compound and 30 g of sodium sulfate at normal temperature and normal pressure to obtain a mixture;
(2)0.1 g of polyacrylamide is added with 1 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S7;
(4) 1 g of FS-S7 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance as shown in Table 4 (example 13).
[ COMPARATIVE EXAMPLE 8 ]
(1) Using 55 g of the long-chain polyether nitrogen-containing compound in example 2, adding no alkylamine polyether carboxylate, and uniformly mixing with 30 g of sodium sulfate, 10 g of sodium carbonate, 30 g of sodium bicarbonate and 30 g of urea at normal temperature and normal pressure to obtain a mixture;
(2) 0.5 g of polyethylene glycol is added with 2 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S8;
(4) 1 g of FS-S8 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance as shown in Table 4 (example 13).
[ COMPARATIVE EXAMPLE 9 ]
(1) 60 g of the long-chain polyether nitrogen-containing compound in the [ example 3 ] is used, and 10 g of urea and 1 g of citric acid are uniformly mixed at normal temperature and normal pressure without adding alkylamine polyether carboxylate to obtain a mixture;
(2) adding 0.1 g of starch and 2 g of water into the mixture, and stirring the mixture until the starch is completely dissolved to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S9;
(4) 1 g of FS-S9 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam drainage agent and the height of the foam after 5 minutes were measured and tested for foam drainage performance as shown in Table 4 (example 13).
[ COMPARATIVE EXAMPLE 10 ]
(1) Using 40 g of long-chain polyether containing nitrogen in [ example 4 ], adding no alkylamine polyether carboxylate compound, and uniformly mixing with 20 g of urea, 5 g of sodium chloride and 1 g of sodium citrate at normal temperature and normal pressure to obtain a mixture;
(2) 0.01 g of polyacrylamide is added with 0.5 g of water and stirred until the polyacrylamide is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S10;
(4) 1 g of FS-S10 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam was measured and the height of the foam after 5 minutes was measured, and the results of the foam drainage performance test were shown in Table 4, as in example 13.
[ COMPARATIVE EXAMPLE 11 ]
(1) 30 g of the long-chain polyether nitrogen-containing compound in the example 5 is used, and is uniformly mixed with 7 g of sodium bicarbonate, 1 g of sodium borate, 2 g of sodium tartrate and 1 g of biuret at normal temperature and normal pressure without adding alkylamine polyether carboxylate to obtain a mixture;
(2)0.1 g of polyethylene glycol is added with 1.0 g of water and stirred until the polyethylene glycol is completely dissolved, so as to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S11;
(4) 1 g of FS-S11 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam was measured and the height of the foam after 5 minutes was measured, and the results of the foam drainage performance test were shown in Table 4, as in example 13.
[ COMPARATIVE EXAMPLE 12 ]
(1) 40 g of the long-chain polyether nitrogen-containing compound in example 6 was used, and 30 g of urea and 1 g of sodium bicarbonate were uniformly mixed at normal temperature and pressure without adding alkylamine polyether carboxylate to obtain a mixture;
(2) adding 0.1 g of cellulose and 1.0 g of water into the mixture, and stirring the mixture until the cellulose is completely dissolved to obtain an adhesive solution;
(3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and performing compression molding to obtain a solid foam drainage rod FS-S12;
(4) 1 g of FS-S12 solid was weighed and dissolved in 100,000, 200,000, 250,000mg/L mineralized simulated aqueous solutions to prepare 5000mg/L solutions, and then the initial height of the foam was measured and the height of the foam after 5 minutes was measured, and the results of the foam drainage performance test were shown in Table 4, as in example 13.
Composition component Structure in the examples of Table 1
Figure BDA0001437211150000121
Foam Properties of the foam drainage agent compositions in the examples of Table 2
Figure BDA0001437211150000131
TABLE 3 foaming Properties of the foam drainage agent compositions of comparative examples 1 to 6
Figure BDA0001437211150000141
TABLE 4 foaming Properties of the foam drainage agent compositions of comparative examples 7 to 12
Figure BDA0001437211150000151

Claims (8)

1. A method of drainage and gas production using a solid foam drainage agent composition comprising the steps of:
(1) throwing the solid foam drainage agent composition into an aqueous gas well;
(2) contacting the solid foamed drainage agent composition with a mixture of gas and water or oil and water in an aqueous gas well sufficient to form a foamed fluid, and then lifting the foamed fluid to the surface;
the solid foam drainage agent composition comprises the following components in parts by weight:
(1)1 part of an alkylamine polyether carboxylate;
(2) 0.1-50 parts of a long-chain polyether nitrogen-containing compound;
(3) 0.2-100 parts of solid filler;
(4)0 to 0.5 parts of a binder, and not including 0 part;
the molecular formula of the alkylamine polyether carboxylate is as follows:
Figure FDA0002931127950000011
wherein R is1Is C8~C20Any one of the alkyl groups of (a); m, n, p and q are any number of 0-20, m + n is more than or equal to 1, X is at least one of alkali metal ions or ammonium ions, m + p is any number of 1-5, and n + q is any number of 5-15.
2. The method of claim 1, wherein the long chain polyether nitrogen compound has the general molecular formula:
Figure FDA0002931127950000012
wherein, R is1Is C10~C26Fatty group of (2)Or C10~C26An aromatic group of (a); y is 0-20, and z is 0-60; r4、R5Is independently selected from C1~C5Alkyl of (C)1~C5Any one of the substituted alkyl groups of (a); r6、R7Is independently selected from C1~C5Alkylene of (C)1~C5Any one of the substituted alkylene groups of (a); y is selected from anionic groups which render the molecule of formula (II) electrically neutral.
3. The method of drainage and gas production using a solid foam drainage agent composition of claim 2, wherein R is1Is C10~C20Alkyl of (C)10~C20Of an alkylbenzene of, R7Is C2H4Or C3H6
4. The method of claim 2 wherein z is greater than 0.
5. The method of claim 1, wherein the solid filler is at least one of an inorganic oxyacid salt, a metal halide, an organic carboxylic acid and its salt, urea, and biuret.
6. The method of draining gas using a solid foam drainage agent composition according to claim 1, characterized in that the solid filler is at least one of carbonate, bicarbonate, sulfate, phosphate, borate, metal halide, formate, acetate, tartaric acid and its salts, citric acid and its salts, phthalic acid and its salts, gallic acid and its salts, urea, biuret.
7. The method of claim 1, wherein the binder is at least one of dextrin, epoxy resin, polyacrylamide, starch, cellulose, polyethylene glycol.
8. The method for draining and producing gas by using the solid foam drainage agent composition according to any one of claims 1 to 7, wherein when the binder is not equal to 0 part, the method for preparing the solid foam drainage agent composition comprises the following steps:
(1) uniformly mixing the alkylamine polyether carboxylate, the long-chain polyether nitrogen-containing compound and the solid filler according to the required mass portion to obtain a mixture;
(2) adding water to the adhesive until the adhesive is completely dissolved to obtain an adhesive solution;
(3) and (3) uniformly mixing the mixture obtained in the step (1) and the adhesive solution obtained in the step (2), and pressing and forming to obtain the solid foam drainage agent composition.
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