CN109401743B - Foam scrubbing agent composition for salt-resistant acid-resistant water drainage and gas production and preparation method and application thereof - Google Patents

Foam scrubbing agent composition for salt-resistant acid-resistant water drainage and gas production and preparation method and application thereof Download PDF

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CN109401743B
CN109401743B CN201710699350.5A CN201710699350A CN109401743B CN 109401743 B CN109401743 B CN 109401743B CN 201710699350 A CN201710699350 A CN 201710699350A CN 109401743 B CN109401743 B CN 109401743B
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acid
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agent composition
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CN109401743A (en
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裘鋆
何秀娟
沈之芹
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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    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
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Abstract

The invention relates to a foam scrubbing agent composition for salt-tolerant acid-tolerant water and gas drainage and a preparation method and application thereof. The method mainly solves the problem that the gas well has reduced production and even stops spraying due to excessive liquid loading in the development process of the existing gas well. The paint comprises the following components in parts by mass: (1)1 part of imidazoline type amphoteric surfactant; (2) 0.2-20 parts of alpha-olefin sulfonate; (3)0-10 parts of nanoparticles; wherein the imidazoline type amphoteric surfactant has a molecular general formula shown in a formula (I), and R is1Is C8~C30The fatty group of (a); r2Is C1~C5Any one of alkylene or substituted alkylene of (a); the technical scheme that Y is an anionic group which enables the molecule shown in the formula (I) to be neutral in electricity better solves the problem and can be suitable for water drainage and gas production of high-salinity acid-containing gas fields.

Description

Foam scrubbing agent composition for salt-resistant acid-resistant water drainage and gas production and preparation method and application thereof
Technical Field
The invention relates to a foam scrubbing agent composition for salt-tolerant acid-tolerant water-draining gas production, a preparation method and application thereof, and belongs to the technical field of oil-gas field chemical agents.
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. 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. The foam drainage is characterized in that a surfactant with special functions is introduced into mineralized water at the bottom of a well, so that a large amount of low-density water-containing foam is generated in the process of gas-liquid two-phase mixing and vertical flowing, the foam carries water along with air flow from the bottom of the well to the ground, the gas-liquid vertical liquid lifting capacity is improved, and the purpose of drainage and gas recovery is achieved. Some gas fields not only have high mineralization degree, but also are acidic due to the existence of acid gas, so that the foaming capacity and stability of the foam discharging agent are greatly reduced, and the effect of water discharging and gas production cannot be achieved. Therefore, it is required to develop an acid-resistant salt-resistant foam discharging agent with high foaming efficiency.
At present, the foaming agent for water drainage and gas production mostly adopts a multi-component compound system and simultaneously comprises a non-ionic surfactant and an ionic surfactant. In order to enhance the stability of a single foam, an auxiliary agent such as alkali, alcohol, polymer, alkanolamide and the like is usually added into the formula to form a reinforced foam. Patent CN102212344A discloses a high-temperature foam discharging agent for drainage and gas production, which comprises the following components in parts by mass: 10-15 parts of sodium dodecyl sulfate, 2-5 parts of alkyl glycoside, 15-18 parts of AES, 20-25 parts of sodium dodecyl sulfate, 5-10 parts of biosurfactant and 27-48 parts of water, and the salt resistance of the composite is poor. 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 having foam discharging and sterilizing functions, and a hydrophobic chain is a hydrophobic segment in substituted naphthalene ring, benzene ring or natural oil ester, so that the foam fluid has strong chlorine resistance and condensate oil resistance, and also has good corrosion inhibition performance. However, since the molecular structure contains an amide group which is sensitive to high temperature, the compound is easily hydrolyzed under acidic conditions.
Disclosure of Invention
One of the technical problems to be solved by the invention is that the existing gas well has excessive liquid accumulation in the development process, so that the yield of the gas well is reduced, and even the gas well stops spraying, and the invention provides the gas well foam discharging agent composition with high liquid carrying efficiency, which has good salt resistance, acid resistance, foaming performance and liquid carrying capacity.
The second technical problem to be solved by the invention is to provide a preparation method of the foam scrubbing agent composition for salt-resistant acid-resistant water drainage gas production, which corresponds to the solution of the first technical problem.
The invention also provides an application method of the foam discharging agent composition for salt-tolerant acid-resistant water and gas drainage and gas production in water drainage and gas production, which corresponds to the solution of one of the technical problems.
In order to solve one of the above technical problems, the technical scheme adopted by the invention is as follows: a foam scrubbing agent composition for salt-tolerant acid-tolerant water and gas drainage comprises the following components in parts by mass:
(1)1 part of imidazoline type amphoteric surfactant;
(2) 0.2-20 parts of alpha-olefin sulfonate;
(3)0-10 parts of nanoparticles;
the imidazoline type amphoteric surfactant has the following molecular general formula:
Figure BDA0001379961450000021
wherein R is1Is C8~C30The fatty group of (a); r2Is C1~C5Any one of alkylene or substituted alkylene of (a); y is an anionic group which renders the molecule of formula (I) electrically neutral.
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 scheme, R1Is C8~C30The aliphatic group (C) may contain a group such as an acyl group, a carbonyl group, an ether group, a hydroxyl group, etc., and may contain a saturated carbon chain or an unsaturated carbon chain, and R is preferably R1Is the preferred embodiment of C8~C18Alkyl of (C)8~C18Alkenyl groups of (a).
In the above technical scheme, R2Preferably C1~C3Alkylene of (C)1~C3Any one of the substituted alkylene groups of (1).
In the above technical solution, the α -olefin sulfonate preferably has the following molecular formula:
R3-HC=CH-CH2-SO3M (II)
wherein R is3Is C5~C30M is any one of gold selected from alkali metalsBelongs to ions; further preferably: m is preferably selected from sodium or potassium ions of alkali metals, more preferably from sodium; r3Preferably selected from C8~C22More preferably selected from C14~C18Alkyl group of (1).
In the above technical scheme, the nanoparticles are at least one of silicon dioxide, hectorite and calcium carbonate.
In the above technical scheme, the acid and salt resistant foam scrubbing agent composition preferably comprises, in parts by weight: (1)1 part of imidazoline type amphoteric surfactant; (2)0.5-10 parts of alpha-olefin sulfonate; (3)1-5 parts of nano particles.
The foaming agent composition of the invention is prepared by using water without special requirements, and can be deionized water or water containing inorganic minerals, wherein the water containing the inorganic minerals can be tap water, gas well formation water or gas well injection water.
To solve the second technical problem, the invention adopts the following technical scheme: a preparation method of an acid-resistant salt-resistant water-draining gas-producing foam discharging agent composition comprises the following steps:
(1) synthesis of imidazoline type amphoteric surfactant
a. Adding R into a reaction kettle1COOH and hydroxyethyl ethylene diamine react to obtain an imidazoline intermediate;
b. adding an imidazoline intermediate and a sulfonation reagent or a carboxylation reagent into a reaction kettle according to a molar ratio of 1 (1-3), and reacting for 1-10 hours at 60-100 ℃ to obtain the imidazoline type amphoteric surfactant, wherein the sulfonation reagent is hydroxysulfonic acid and salts thereof, and halogenated sulfonic acid and salts thereof; the carboxylation reagent is halogenated carboxylic acid and salt thereof;
(2) preparation of foam discharging agent composition
Dissolving imidazoline type amphoteric surfactant, alpha-olefin sulfonate and nano particles in water according to the required mass ratio, and uniformly mixing to obtain the salt-resistant acid-resistant water-discharging gas-collecting foam discharging agent composition.
In the technical scheme, the reaction in the step a is preferably heated to 100 ℃, the vacuum degree of the reaction kettle is adjusted to be in a water outlet state, then the temperature is continuously raised to 200 ℃, and the reaction is carried out for 6 hours, so as to obtain the imidazoline intermediate.
The key active ingredients of the foam discharging agent are alpha-olefin sulfonate and imidazoline type amphoteric surfactant, and the technical personnel in the field know that the foam discharging agent can adopt various supply forms for the aspects of transportation and storage or field use, such as non-aqueous solid form, aqueous paste form or aqueous solution form; the water solution form comprises a form of preparing concentrated solution by water and directly preparing a foam discharging agent form with the concentration required on site; the water is not particularly required, and can be deionized water or water containing inorganic minerals, and the water containing the inorganic minerals can be tap water, gas well formation water or gas well injection water.
In order to solve the third technical problem, the technical scheme adopted by the invention is as follows: an application method of a foam discharging agent composition for salt-tolerant acid-tolerant water and gas drainage and gas production in water and gas drainage and gas production.
In the above technical scheme, the application method is not particularly limited, and those skilled in the art can apply the method according to the drainage gas production process technology in the prior art, for example, but not limited to, the salinity of formation water applicable to the gas well is 0 to 200000ppm, and the applicable pH value is 3 to 7.
The imidazoline-type amphoteric surfactant of the acid-resistant salt-tolerant water drainage gas production foam discharging agent is an excellent foaming agent, has good foaming performance and salt resistance, is insensitive to pH value due to the fact that the imidazoline-type amphoteric surfactant is zwitterion, has good acid resistance, and has good synergistic effect with an anionic surfactant; the alpha-olefin sulfonate has good foaming capacity and good salt resistance, and the alpha-olefin sulfonate form a compounding synergistic effect after being mixed, so that the liquid carrying capacity and the foam stabilizing performance of the foam are enhanced; the addition of the nano particles can effectively increase the viscosity of a foam system, form a compact granular film and inhibit the coalescence and disproportionation of bubbles, thereby enhancing the stability of the foam.
By adopting the technical scheme, the foam scrubbing agent composition can be suitable for gas wells with the mineralization degree lower than 200000mg/L and the pH value of 3-7. The foam performance test of the foam scrubbing agent is carried out according to SY/T6465-2000 foamer evaluation method for foam drainage and gas recovery, the foaming height is more than 200mm, the liquid carrying amount is more than 140mL, and the foam scrubbing agent has good foaming performance, foam stability and liquid carrying capacity and obtains better technical effects.
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.
Detailed Description
[ example 1 ]
Preparation of composition XN-1, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. Adding 25 g of C into a reaction kettle12H25Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 7.5 g of sodium chloroacetate into a reaction kettle, and reacting for 5 hours at 80 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS14-16Dissolving silicon dioxide and water with the mineralization degree of 50000mg/L and the pH value of 7 according to the mass ratio of 1:1:1, uniformly mixing, and preparing into 1.0 wt% solution to obtain the foam scrubbing agent composition XN-1. The component structure is shown in table 1.
[ example 2 ]
Preparation of composition XN-2, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. Adding 23 g of C into a reaction kettle14H27Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 10 g of chloropropyl sodium sulfonate into a reaction kettle, and reacting for 6 hours at 80 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS14-18Dissolving silicon dioxide and water with the mineralization degree of 150000mg/L and the pH value of 3 according to the mass ratio of 1:5:4, and uniformly mixing to prepare a 1.0 wt% solution, thus obtaining the foam scrubbing agent composition XN-2. The component structure is shown in table 1.
[ example 3 ]
Preparation of composition XN-3, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 18 g of C are added into a reaction kettle10H21Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 8.5 g of sodium chloropropionate into a reaction kettle, and reacting for 3 hours at 100 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS16-18Dissolving silicon dioxide and water with the mineralization degree of 80000mg/L and the pH value of 5 in a mass ratio of 1:2:3, and uniformly mixing to prepare 1.0 wt% solution, namely the foam scrubbing agent composition XN-3. The component structure is shown in table 1.
[ example 4 ]
Preparation of composition XN-4, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 32 g of C are added into a reaction kettle16H33Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 9 g of chloroethyl sodium sulfonate into a reaction kettle, and reacting for 6 hours at 60 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS14-16Dissolving silicon dioxide in water with the mineralization of 100000mg/L and the pH value of 5 according to the mass ratio of 1:0.5:3, uniformly mixing, and preparing into 1.0 wt% solution to obtain the foam scrubbing agent composition XN-4. The component structure is shown in table 1.
[ example 5 ]
Preparation of composition XN-5, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 30 g of C are added into a reaction kettle18H35Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 8 g of chloroethyl sodium sulfonate into a reaction kettle, and reacting for 3 hours at 100 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS14-18Dissolving silicon dioxide and water with the mineralization degree of 100000mg/L and the pH value of 3 according to the mass ratio of 1:10:5, and uniformly mixing to prepare 1.0 wt% solution, thus obtaining the foam scrubbing agent composition XN-5. The component structure is shown in table 1.
[ example 6 ]
Preparation of composition XN-6, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 20 g of C are added into a reaction kettle12H23Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 8.5 g of sodium chloroacetate into a reaction kettle, and reacting for 8 hours at 60 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS16-18Dissolving silicon dioxide and water with the mineralization degree of 150000mg/L and the pH value of 5 according to the mass ratio of 1:3:4, and uniformly mixing to prepare a 1.0 wt% solution, thus obtaining the foam scrubbing agent composition XN-6. The component structure is shown in table 1.
[ example 7 ]
Preparation of composition XN-7, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 20 g of C are added into a reaction kettle12H25Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 10 g of sodium chlorobutyrate into a reaction kettle, and reacting for 7 hours at 60 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS14-16Dissolving silicon dioxide in water with the mineralization of 100000mg/L and the pH value of 3 according to the mass ratio of 1:0.8:5, uniformly mixing, and preparing into 1.0 wt% solution to obtain the foam scrubbing agent composition XN-7. The component structure is shown in table 1.
[ example 8 ]
Preparation of composition XN-8, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 16 g of C are added into a reaction kettle8H17Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 10 g of sodium chloropropionate into a reaction kettle, and reacting for 4 hours at 80 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS16-18And hectorite are dissolved in water with the mineralization of 100000mg/L and the pH value of 7 according to the mass ratio of 1:8:2, and the mixture is uniformly mixed to prepare 1.0 wt% solution, thus obtaining the foam discharging agent composition XN-8. The component structure is shown in table 1.
[ example 9 ]
Preparation of composition XN-9, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 19 g of C are added into a reaction kettle10H19Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 19 g of chloroethyl sodium sulfonate into a reaction kettle, and reacting for 5 hours at 80 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS16-18Dissolving calcium carbonate and water with the mineralization of 200000mg/L and the pH value of 3 in a mass ratio of 1:9:1, and mixing uniformly to prepare a 1.0 wt% solution, thus obtaining the foam scrubbing agent composition XN-9. The component structure is shown in table 1.
[ example 10 ]
Preparation of composition XN-10, preparation procedure:
(1) synthesis of imidazoline type amphoteric surfactant
a. 20 g of C are added into a reaction kettle12H25Heating COOH and 10 g of hydroxyethyl ethylenediamine to 100 ℃, adjusting the vacuum degree of the reaction kettle to a water outlet state, continuing heating to 200 ℃, reacting for 6 hours, and stopping the reaction to obtain an imidazoline intermediate;
b. adding 15 g of imidazoline intermediate obtained by reaction and 9 g of sodium chloropropionate into a reaction kettle, and reacting for 4 hours at 80 ℃ to obtain the imidazoline type amphoteric surfactant;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant and AOS16-18Dissolving in water with mineralization of 200000mg/L and pH of 3 at a mass ratio of 1:2, mixing well, and making into 1.0 wt% solution to obtain the foam discharging agent composition XN-10. The component structure is shown in table 1.
[ example 11 ]
The performances of the foam discharging agent such as foaming power, foam stability, liquid carrying capacity and the like are measured according to SY/T6465-2000 evaluation method for foam drainage and gas production foaming agent. The results are shown in Table 2.
[ COMPARATIVE EXAMPLE 1 ]
Using the imidazoline type amphoteric surfactant synthesized in example 1 and nano-silica without adding α -olefin sulfonate, dissolved in 50000mg/L of mineralization and pH 7 water at a mass ratio of 1:1, mixed uniformly to prepare a 1.0 wt% solution, to prepare a foam discharging agent composition, and the foam discharging performance test was performed as in example 11, and the results are shown in table 3.
[ COMPARATIVE EXAMPLE 2 ]
Using the α -olefin sulfonate and nanosilica in [ example 1 ], without adding a synthetic imidazoline type amphoteric surfactant, dissolved in 50000mg/L of mineralization and pH 7 at a mass ratio of 1:1, and mixed uniformly to prepare a 1.0 wt% solution, a foam discharging composition was prepared, and the foam discharging performance test was performed as in [ example 11 ], and the results are shown in table 3.
[ COMPARATIVE EXAMPLE 3 ]
The imidazoline type amphoteric surfactant, petroleum sulfonate and silicon dioxide prepared in example 1 were dissolved in water having a mineralization of 50000mg/L and a pH of 7 at a mass ratio of 1:1:1, mixed uniformly to prepare a 1.0 wt% solution, and a foam drainage performance test was performed in the same manner as in example 11, and the results are shown in table 3.
[ COMPARATIVE EXAMPLE 4 ]
The imidazoline type amphoteric surfactant prepared in example 1, sodium lauryl sulfate, and silicon dioxide were dissolved in water having a mineralization of 50000mg/L and a pH of 7 at a mass ratio of 1:1:1, and mixed uniformly to prepare a 1.0 wt% solution, to prepare a foam discharging agent composition, and a foam discharging performance test was performed in the same manner as in example 11, and the results are shown in table 3.
[ COMPARATIVE EXAMPLE 5 ]
The imidazoline type amphoteric surfactant prepared in example 1, sodium oleate and silicon dioxide were dissolved in water having a mineralization of 50000mg/L and a pH of 7 at a mass ratio of 1:1:1, and mixed uniformly to prepare a 1.0 wt% solution, to prepare a foam discharging agent composition, and a foam discharging performance test was performed as in example 11, and the results are shown in table 3.
Table 1 compositional structure of foam remover compositions in the examples
Foaming agent R1 R2 Y AOS Nanoparticles Mass ratio of I to II to nanoparticles Degree of mineralization mg/L pH value
XN-1 C12H25 CH2 COO- AOS14-16 Silicon dioxide 1:1:1 50000 7
XN-2 C14H27 C3H6 SO3 - AOS14-18 Silicon dioxide 1:5:4 150000 3
XN-3 C10H21 C2H4 COO- AOS16-18 Silicon dioxide 1:2:3 80000 5
XN-4 C16H33 C2H4 SO3 - AOS14-16 Silicon dioxide 1:0.5:3 100000 5
XN-5 C18H35 C2H4 SO3 - AOS14-18 Silicon dioxide 1:10:5 100000 3
XN-6 C12H23 CH2 COO- AOS16-18 Silicon dioxide 1:3:4 150000 5
XN-7 C12H25 C3H6 COO- AOS14-16 Silicon dioxide 1:0.8:5 100000 3
XN-8 C8H17 C2H4 COO- AOS16-18 Hectorite 1:8:2 100000 7
XN-9 C10H19 C2H4 SO3 - AOS16-18 Calcium carbonate 1:9:1 200000 3
XN-10 C12H25 C2H4 COO- AOS16-18 / 1:2:0 200000 3
Foam properties of the foam remover compositions in the examples of Table 2
Foam scrubbing agent composition Height mm of Roche blister 5min foam height mm Liquid carrying capacity mL
XN-1 279 259 178
XN-2 240 236 157
XN-3 275 256 170
XN-4 269 253 168
XN-5 260 249 167
XN-6 241 236 160
XN-7 270 252 169
XN-8 266 254 166
XN-9 234 230 152
XN-10 239 220 150
TABLE 3 foam Properties of the foam remover compositions of the comparative examples
Foam scrubbing agent Height mm of Roche blister 5min foam height mm Liquid carrying capacity mL
Comparative example 1 131 110 95
Comparative example 2 101 65 20
Comparative example 3 153 124 103
Comparative example 4 105 70 20
Comparative example 5 50 36 0

Claims (9)

1. A foam scrubbing agent composition for salt-tolerant acid-tolerant water and gas drainage comprises the following components in parts by mass:
(1)1 part of imidazoline type amphoteric surfactant;
(2) 0.2-20 parts of alpha-olefin sulfonate;
(3)1-10 parts of nanoparticles;
the imidazoline type amphoteric surfactant has the following molecular general formula:
Figure FDA0002928962850000011
wherein R is1Is C8~C30The fatty group of (a); r2Is C1~C5Any one of alkylene or substituted alkylene of (a); y is an anionic group which renders the molecule of formula (I) electrically neutral;
the alpha-olefin sulfonate has the following molecular formula:
R3-HC=CH-CH2-SO3M, (II);
in the formula R3Is C5~C30M is any one metal ion selected from alkali metals.
2. The foam scrubbing composition for salt and acid tolerant drainage and gas generation as claimed in claim 1, wherein R is selected from the group consisting of1Is selected from C8~C18Alkyl of (C)8~C18Alkenyl of (a); r2Is selected from C1~C3Alkylene of (C)1~C3Any one of the substituted alkylene groups of (a); y is selected from-COO、-SO3 、-HPO4 At least one of (1).
3. The foam scrubbing composition for salt and acid tolerant water and gas recovery as claimed in claim 1, wherein Y is selected from the group consisting of-COO、-SO3 At least one of (1).
4. The salt and acid tolerant drainage of claim 1The gas-collecting foam discharging agent composition is characterized in that R is3Is selected from C8~C22Alkyl group of (1).
5. The foam scrubbing composition according to claim 1, wherein said nanoparticles are at least one of nano-silica, nano-laponite, and nano-calcium carbonate.
6. The foam discharging agent composition for salt and acid resistant drainage and gas production according to claim 1, which is characterized by comprising the following components in parts by weight: (1)1 part of imidazoline type amphoteric surfactant; (2)0.5-10 parts of alpha-olefin sulfonate; (3)1-5 parts of nano particles.
7. A preparation method of the foam scrubbing agent composition for gas production for salt-tolerant acid-tolerant drainage as claimed in any one of claims 1 to 6, comprising the following steps:
(1) synthesis of imidazoline type amphoteric surfactant
a. Adding R into a reaction kettle1COOH and hydroxyethyl ethylene diamine react to obtain an imidazoline intermediate;
b. adding an imidazoline intermediate and a sulfonation reagent or a carboxylation reagent into a reaction kettle according to a molar ratio of 1 (1-3), and reacting for 1-10 hours at 60-100 ℃ to obtain the imidazoline type amphoteric surfactant shown in the formula (I), wherein the sulfonation reagent is hydroxysulfonic acid and salts thereof, halogenated sulfonic acid and salts thereof; the carboxylation reagent is halogenated carboxylic acid and salt thereof;
(2) preparation of foam discharging agent composition
Mixing imidazoline type amphoteric surfactant, alpha-olefin sulfonate and nano particles with water uniformly according to the required mass portion to obtain the salt-resistant acid-resistant water-discharging gas-collecting foam discharging agent composition.
8. Use of the foam discharging agent composition for salt-tolerant acid-tolerant water and gas drainage of any one of claims 1 to 6 in water and gas drainage.
9. The application of the foam discharging agent composition for the salt and acid resistant drainage and gas production in the drainage and gas production according to claim 8 is characterized in that the salinity of formation water of a suitable gas well is 0-200000 ppm, and the suitable pH value is 3-7.
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CN116410725A (en) * 2021-12-29 2023-07-11 中国石油天然气股份有限公司 Corrosion inhibition type foam discharging agent for gas field, preparation method and application
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102676142A (en) * 2012-05-28 2012-09-19 中国石油天然气股份有限公司 Condensate oil foam discharging agent suitable for natural gas exploitation
CN103254884A (en) * 2013-05-27 2013-08-21 上海大学 High-efficient foam compound flooding agent for tertiary oil recovery and preparation method thereof
CN103289666A (en) * 2013-06-04 2013-09-11 西南石油大学 Automatic-defoaming foam discharging agent for gas well drainage and preparation method thereof
CN103881683A (en) * 2014-02-26 2014-06-25 中国石油化工股份有限公司 Foaming agent for plugging gas channeling in displacement of reservoir oil by using CO2
WO2017086918A1 (en) * 2015-11-16 2017-05-26 Halliburton Energy Services, Inc. Alkyl polyglycoside surfactants for use in subterranean formations

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102676142A (en) * 2012-05-28 2012-09-19 中国石油天然气股份有限公司 Condensate oil foam discharging agent suitable for natural gas exploitation
CN103254884A (en) * 2013-05-27 2013-08-21 上海大学 High-efficient foam compound flooding agent for tertiary oil recovery and preparation method thereof
CN103289666A (en) * 2013-06-04 2013-09-11 西南石油大学 Automatic-defoaming foam discharging agent for gas well drainage and preparation method thereof
CN103881683A (en) * 2014-02-26 2014-06-25 中国石油化工股份有限公司 Foaming agent for plugging gas channeling in displacement of reservoir oil by using CO2
WO2017086918A1 (en) * 2015-11-16 2017-05-26 Halliburton Energy Services, Inc. Alkyl polyglycoside surfactants for use in subterranean formations

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
新型气井泡排剂SP的起泡性能研究;刘竟成 等;《油田化学》;20080625;第25卷(第2期);第112-113页第2.1节、第2.3节、表3,第114页第3节 *
纳米颗粒稳定泡沫在油气开采中的研究进展;杨兆中 等;《化工进展》;20170609;第36卷(第5期);第1676页右栏第3段,第1676-1677页第1.1-1.2节 *

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