CN109679617B - Solid foam drainage agent composition suitable for ultra-deep gas well, preparation method and application - Google Patents

Solid foam drainage agent composition suitable for ultra-deep gas well, preparation method and application Download PDF

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CN109679617B
CN109679617B CN201710969820.5A CN201710969820A CN109679617B CN 109679617 B CN109679617 B CN 109679617B CN 201710969820 A CN201710969820 A CN 201710969820A CN 109679617 B CN109679617 B CN 109679617B
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foam drainage
hydrocarbyl
sodium
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CN109679617A (en
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沈之芹
李应成
何秀娟
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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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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • 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
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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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    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
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Abstract

The invention relates to a solid foam drainage agent composition suitable for an ultra-deep gas well, a preparation method and application thereof, and mainly solves the problem that the existing foam drainage agent contains H2S、CO2The high-temperature and high-salt resistance in an acidic environment is poor, and the problems of production reduction, even spray stopping and difficult filling of the liquid foam discharging agent caused by liquid loading of a high-temperature and high-salt ultra-deep gas well cannot be solved. The solid foam scrubbing agent composition comprises the following components in parts by mass: (1)1 part of polyamine polyether compound; (2) 0.01-100 parts of cosurfactant; (3) 0.05-1000 parts of solid filler; (4) 0-0.5 parts of adhesive; the polyamine polyether compound has a general molecular formula shown in formula (1): the cosurfactant has at least one of the molecular general formula shown in the formula (2) or the molecular general formula shown in the formula (3), so that the problem is solved well, and the cosurfactant can be used for drainage gas recovery of an acidic high-temperature high-salt ultra-deep gas well.

Description

Solid foam drainage agent composition suitable for ultra-deep gas well, preparation method and application
Technical Field
The invention relates to a solid foam drainage agent composition, a preparation method and application thereof, in particular to a solid foam drainage agent composition suitable for an ultra-deep gas well, a preparation method and application thereof.
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. 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 slipped and deposited 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 the shaft, so that the accumulated liquid in the shaft is discharged, and the purposes of water drainage and gas production are achieved.
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 reinforced 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, and the drainage effect and use concentration are not referred to in the patent. 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 both foam drainage and sterilization functions, a hydrophobic chain is a hydrophobic segment in substituted naphthalene ring, benzene ring or natural oil ester, and has strong chlorine resistance and condensate oil resistance, and also has good corrosion inhibition performance, the foam agent with an active matter concentration of 400ppm has a foam drainage rate of 86.8% in tap water and a foam drainage rate of 79.1% in simulated brine with a mineralization degree of 130000mg/L, however, because an amide group sensitive to high temperature is contained in a molecular structure, the foam fluid has poor adaptability to gas wells with a temperature of more than 100 ℃. China is a technology for researching foam drainage and gas production processes 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, and the amount of the foaming agent is 5000ppm, but the agent contains the fluorocarbon surfactant, so that not only the cost is greatly improved, but also the environmental impact is large.
The results show that the poor high-temperature and high-salt resistance is a main factor for restricting the development of the foam drainage technology of the high-temperature ultra-deep gas well.
Disclosure of Invention
The invention aims to solve the technical problems that the existing foam drainage agent has poor high-temperature resistance in an acid environment, cannot solve the problems of yield reduction and even spray stopping caused by liquid accumulation of a high-temperature ultra-deep gas well and difficulty in filling a liquid foam drainage agent, and provides a solid foam drainage agent composition suitable for the ultra-deep gas well, which is applied to a high-temperature deep well, has very good temperature resistance under an acid condition, and has strong liquid carrying, foaming and foam stabilizing properties.
The second technical problem to be solved by the present invention is to provide a method for preparing a solid foam drainage agent composition suitable for ultra-deep gas wells, which corresponds to the solution of the first technical problem.
The third technical problem to be solved by the present invention is to provide a solid foam drainage agent composition for ultra-deep gas wells, which corresponds to the solution of one of the above technical problems.
In order to solve one of the above technical problems, the technical scheme adopted by the invention is as follows: the solid foam water discharging agent composition suitable for the ultra-deep gas well comprises the following components in parts by weight:
(1)1 part of polyamine polyether compound;
(2) 0.01-100 parts of cosurfactant;
(3) 0.05-1000 parts of solid filler;
(4) 0-0.5 parts of adhesive;
wherein the polyamine polyether compound has a general molecular formula shown in formula (1):
Figure BDA0001437255110000021
in the formula (1), R1Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R2、R3、R4Independently selected from H, C1~C5Hydrocarbyl or substituted hydrocarbyl carboxylates, C1~C5Alkyl or substituted alkyl sulfonates, C1~C5Hydrocarbyl or substituted hydrocarbyl phosphates or C1~C5At least one of alkyl sulfate or substituted alkyl sulfate, which is not H at the same time; m is-N (A) CH2CH2-the number of fragments, m ═ 1 to 10; a is a substituent represented by the formula (3); s1, s2 and s3 are addition numbers of propoxy groups PO, s1 is 0-30, s2 is 0-30, s0-30% of 3; r1, r2 and r3 are the addition number of ethoxy EO, r1 is 0-30, r2 is 0-30, r3 is 0-30, and s1+ s2+ m s3 and r1+ r2+ m r3 are not zero at the same time;
Figure BDA0001437255110000031
in the above technical solution, the cosurfactant is preferably at least one selected from a zwitterionic surfactant, a cationic surfactant and an anionic surfactant; the zwitterionic or cationic surfactant preferably has a general molecular formula shown in formula (2):
Figure BDA0001437255110000032
in the formula (2), R5Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R6、R7Independently selected from (CH)2)aOH、(CH2)bCH3Or C6H5CH2One of (1), R8Is selected from (CH)2)aOH、(CH2)bCH3、C6H5CH2、(CH2)cOr (CH)2)c(CHOH)d(CH2)eWherein a is any integer from 2 to 4, b is any integer from 0 to 5, c is any integer from 1 to 4, d is any integer from 0 to 3, and e is any integer from 1 to 4; n is the addition number of propoxy groups PO, and n is 0-15; p is the addition number of an ethoxy group EO, and p is 0-30; x-Is selected from OH-Halogen anion, HCO3 -、NO3 -、CH3OSO3 -、CH3COO-、COO-、SO3 -Or OSO3 -One of (1);
the anionic surfactant preferably has a general molecular formula represented by formula (3):
Figure BDA0001437255110000033
in the formula (3), R9And R10The sum is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, M is selected from hydrogen, alkali metal or of the formula NR11(R12)(R13)(R14) At least one of the groups shown, R11、R12、R13、R14Is independently selected from H, (CH)2)aOH or (CH)2)bCH3Wherein a is any integer of 2-4, and b is any integer of 0-5.
In the above technical solution, the solid filler is at least one of carbonate, bicarbonate, sulfate, phosphate, borate, metal halide, formate, acetate, tartaric acid and salts, citric acid and salts, phthalic acid and salts, gallic acid and salts, 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 scheme, R1、R5Preferably C8~C24Hydrocarbyl or substituted hydrocarbyl. In the above technical scheme, R2、R3、R4Independently preferably H, CH2COOM1、(CH2)3SO3M1Or CH2(CHOH)CH2SO3M1And is not simultaneously H.
In the above technical scheme, R6、R7Preferably CH3、C2H5、(CH2)2OH or C6H5CH2One kind of (1).
In the above technical scheme, R8Preferably CH3、C2H5、(CH2)2OH or C6H5CH2One of (1); or R8X-Preferably CH2COO-、(CH2)3SO3 -、CH2(CHOH)CH2SO3 -One kind of (1).
In the above technical scheme, R9And R10The sum is preferably C7~C23Hydrocarbyl or substituted hydrocarbyl.
In the above technical scheme, M and M1Independently preferably hydrogen, an alkali metal or a compound of the formula NR11(R12)(R13)(R14) At least one of the groups shown.
In the above technical scheme, R11、R12、R13、R14Preferably H, (CH)2)aOH or (CH)2)bCH3One kind of (1).
In the above technical means, a is preferably 2 to 4, and b is preferably 0 to 5.
In the above-mentioned technical means, m is preferably 1 to 5.
In the technical scheme, n is preferably 0-5; p is 0 to 5.
In the above technical solution, preferably, s1+ s2+ m s3 is 0 to 5, r1+ r2+ m r3 is 0 to 10, and s1+ s2+ m s3 and r1+ r2+ m r3 are not zero at the same time; more preferably, s1+ s2+ m s3 is 1 to 5, and r1+ r2+ m r3 is 1 to 10.
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.
In the technical scheme, the mass ratio of the polyamine polyether compound, the cosurfactant, the solid filler and the adhesive in the solid foam drainage agent is 1: 0.1-10: 0.1-200: 0.01-0.1.
The key active ingredients of the solid foam discharging agent composition of the invention are (1) and (2), and the solid foam discharging agent composition can be obtained by mixing the polyamine polyether compound, the solid filler and the binder according to a required proportion, and is preferably obtained by the following technical scheme for solving two technical problems.
To solve the second technical problem, the invention adopts the following technical scheme: a method for preparing a solid foam drainage agent composition suitable for an ultra-deep gas well, which solves one of the above technical problems, comprises the following steps:
(1) preparation of polyamine polyether compounds
a. Amidation reaction:
r is to be0COOR' and H (NHCH)2CH2)mNH2Mixing the catalyst in a molar ratio of 1: 1-2: 0-0.5, reacting at a reaction temperature of 50-200 ℃ for 3-15 hours while stirring, and evaporating alcohol or water generated by the reaction under normal pressure or reduced pressure to obtain the desired amide compound R0CO(NHCH2CH2)mNH2(ii) a Wherein R is0Is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, R' is selected from H and C1~C8C is 1-10, and the catalyst is at least one selected from alkali metal hydroxide, alkali metal alkoxide and alkali metal carbonate;
b. reduction reaction:
R0CO(NHCH2CH2)mNH2the reduction of the lactam can be carried out by catalytic hydrogenation, heterogeneous catalytic reaction at high temperature and high pressure to generate the corresponding amine, or by the following steps: the R synthesized in the step a0CO(NHCH2CH2)mNH2With metal hydrides H-Y+Reduction in an aprotic solvent to give R0CH2(NHCH2CH2)mNH2. Wherein, Y+Is a metal compound, a metal alkyl compound, a metal amino compound;
c. and (3) polyether esterification:
in the presence of a basic catalyst, the R synthesized in the step b0CH2(NHCH2CH2)mNH2Sequentially reacting with required amount of propylene oxide and ethylene oxide to obtain long-chain polyamine polyether intermediate product
R0CH2{N[(CHCH3CH2O)s3(CH2CH2O)r3H][CH2CH2]}mN[(CHCH3CH2O)s1(CH2CH2O)r1H][CHCH3CH2O)s2(CH2CH2O)r2)H];
d. Carboxylation or sulfonation reaction:
c, reacting the long-chain polyamine polyether intermediate product obtained in the step c with an ionizing reagent and alkali in a solvent according to the molar ratio of 1: 1-5: 1-10 at the reaction temperature of 50-120 ℃ for 3-20 hours to generate polyamine polyether carboxylate or polyamine polyether sulfonate shown in the structural formula (1); the ionizing agent is selected from XR15Y1Or X R'15Y′1At least one of; the base is selected from alkali metal hydroxide or alkali metal alkoxide; y is1And Y'1Is SO3M1Or COON1,M1And N1Is an alkali metal, and X is chlorine, bromine or iodine;
(2) uniformly mixing the polyamine polyether compound synthesized in the step (1), the cosurfactant, the solid filler and the adhesive according to the required mass parts, and then pressing and forming to prepare the solid foam drainage agent composition.
In the above-described aspect, the solid foam drainage agent composition may have a shape of a bar, a ball, or the like.
In the above technical scheme, R in the step a1COOR’、H(NHCH2CH2)mNH2The molar ratio of the catalyst is preferably 1: 1-1.3: 0-0.1.
In the above technical scheme, the catalyst in step a is preferably at least one of sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate.
In the above technical scheme, step b is H-Y+Preferably LiAlH4、LiAlH(OEt)3Or NaBH4At least one of (1).
In the above technical solution, the aprotic solvent in step b is preferably at least one of diethyl ether, tetrahydrofuran, and dioxane.
In the above technical scheme, the long-chain polyamine polyether intermediate in step d: ionizing agent: the molar ratio of the alkali is preferably 1: (1-2): (1-4).
In the above technical scheme, the solvent in the step d is preferably selected from C3~C8Ketone and C6~C9For example, at least one of the group consisting of acetone, butanone, pentanone, benzene, toluene or xylene, trimethylbenzene, ethylbenzene and diethylbenzene.
In the above technical solution, the XR15Y1Or X R'15Y′1Examples of (b) include, but are not limited to, alkali metal salts of chloroacetic acid, alkali metal salts of bromoacetic acid, alkali metal salts of 3-chloro-2-hydroxypropanesulfonic acid, alkali metal salts of 2-chloroethanesulfonic acid, and the like.
The solid foam water-discharging agent composition suitable for the ultra-deep gas well has good compatibility, and can also contain other treating agents commonly used in the field.
In order to solve the third technical problem, the technical scheme adopted by the invention is as follows: the application of the solid foam water drainage agent composition suitable for the ultra-deep gas well in any one of the technical schemes in drainage and gas production of the acidic high-temperature high-salinity ultra-deep gas well.
In the above technical scheme, the application of the foam drainage agent is not particularly limited, and those skilled in the art can apply the foam drainage agent according to the existing drainage and gas production process technology, for example, but not limited to, the high-temperature acid gas-containing gas reservoir is preferred, the formation temperature is 150-200 ℃, the total mineralization of formation brine is 5000-200000 mg/L, and H is2S and CO2The content of (A) is 0-35%.
The long-chain polyamine compound containing stable chemical bonds can avoid hydrolysis under acidic high-temperature and high-salt conditions, maintain the stability of a molecular structure and maintain the foam drainage capability of the foam drainage agent to the maximum extent. The invention relates to a solid foam water discharging agent composition suitable for an ultra-deep gas well, a preparation method and application thereof in water discharging and gas production.
The thermal decomposition temperature of the polyamine polyether compound prepared by the invention is 200 ℃ or above, the polyamine polyether compound is not hydrolyzed or is hydrolyzed in a trace amount in an acidic aqueous solution, and the polyamine polyether compound has good temperature resistance; nonionic fragments and multi-hydrophilic groups in molecules 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 liquid carrying amount of the foam is increased, and the liquid separation is slowed down; secondly, the foam water discharging agent simultaneously has functional groups with opposite electric property of negative and positive, so that the adsorption capacity of the foam agent on a gas-liquid interface is increased, and the formed composition is more efficient; in addition, the molecule contains hetero atoms responding to pH, so that the molecular sieve can be applied to the drainage and gas production process of acidic high-temperature high-salt ultra-deep wells with the temperature of 150 ℃ and above at low concentration.
The key effective components of the foam discharging agent, the solid filler and the adhesive have good compatibility, and the formed solid composition does not influence the foam discharging performance.
In the present invention, the content or concentration of the foam discharging agent refers to the total content or total concentration of the components (1) and (2) in the above technical scheme. By adopting the technical scheme of the invention, the foam performance test of the foam drainage agent is carried out according to SY/T6465-2000 foamer evaluation method for foam drainage and gas production, the foaming height reaches 175mm and the liquid carrying rate reaches 93.9 percent before and after high-temperature aging when 0.02-0.12 percent of the foam drainage agent is in 0-200,000 mg/L salinity brine, and the foam drainage agent has excellent temperature resistance, salt tolerance, foaming and liquid carrying performances in an acidic environment, thereby obtaining better technical effects.
The invention is further illustrated by the following examples.
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) Preparation of foam scrubbing agent FMG01
a. A reaction flask equipped with mechanical stirring, thermometer, dropping funnel and atmospheric distillation was charged with 127.6 g (0.55 mol) of pentaethylenehexamine and 1.4 g (0.0 mol)25 mol) of potassium hydroxide solid, slowly dripping 148 g (0.5 mol) of methyl oleate while stirring, reacting at the reaction temperature of 120-160 ℃ for 6 hours, and collecting methanol generated by the reaction to obtain the required amide compound C17H33CO(NHCH2CH2)5NH2The yield thereof was found to be 93.8%.
b. Removing water from a three-neck flask device provided with a reflux condenser tube, a dropping funnel and a thermometer, adding 11.4 g (0.3 mol) of lithium aluminum hydride and 90 ml of dry dioxane, stirring, dispersing and mixing, and dropping 49.6 g (0.1 mol) of C at-10-5 DEG C17H33CO(NHCH2CH2)5NH2The 40 wt% dioxane solution is added dropwise and slowly heated to about 35 ℃ for reaction for 3 hours. Carefully pouring the reaction solution into ice water, and carrying out post-treatment to obtain a long-chain polyamine compound C17H33CH2(NHCH2CH2)5NH2The yield thereof was found to be 89.0%.
c. A pressure reactor equipped with a stirring device was charged with 192.8 g (0.4 mol) of C17H33CH2(NHCH2CH2)5NH24.0 g of potassium hydroxide, 469.8 g (8.1 mol) of propylene oxide and 52.8 g (1.2 mol) of ethylene oxide react sequentially at 140-160 ℃ to obtain the long-chain polyamine polyether compound1(R1=C18H35,m=5,s1+s2+5s3=20,r1+r2+5r3=3,R2=R3=R4H), yield 96.2%.
d. Long-chain polyamine polyether compounds1(R1=C18H35,m=5,s1+s2+5s3=20,r1+r2+5r3=3,R2=R3=R4H)177.4 g (0.1 mol) were mixed with 8.0 g (0.2 mol) of sodium hydroxide, 29.5 g (0.15 mol) of sodium 3-chloro-2-hydroxypropanesulfonate and 300 ml of toluene/benzene (v/v ═ 1) in a four-neck flask equipped with a mechanical stirrer, a thermometer and a reflux condenser, and heated to 90 ℃ for 7 hours. Evaporating the solvent to obtain the long-chain polyamine polyether compound1(R1=C18H35,m=5,s1+s2+5s3=20,r1+r2+5r3=3)Sodium hydroxypropanesulfonate (R)2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remainder H).
e. Long-chain polyamine polyether compound1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g, sodium tartrate 100 g, sodium chloride 90 g and urea 30 g are mixed evenly, 10% cellulose water solution 30 g is added for mixing and then pressed into a rod shape, and the foam drainage rod FMG01 is prepared.
(2) FMG01 was dissolved in deionized water, 100,000mg/L, 200,000mg/L NaCl water, respectively, to make up a 0.3 wt% stock solution of the foam-eliminating agent.
The performances of foaming power, foam stability, liquid carrying capacity and the like of the FMG01 solution are determined according to SY/T6465-2000 evaluation method for foam drainage and gas production foamer, and the results are shown in Table 1.
The experiment is carried out by adopting a pressure-resistant and acid-resistant aging device, and the performances such as foaming power, foam stability, liquid carrying capacity and the like are measured again after aging is carried out for 24 hours at 180 ℃, and the results are shown in table 1.
[ example 2 ]
The same as [ example 1 ] except that in the measurement of FMG01 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid to simulate neutral and acid gas environments, and the results are shown in table 2.
[ example 3 ]
The same as [ example 1 ] except that a long-chain polyamine polyether compound is used1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-50 g, 100 g of sodium sulfate, 50 g of potassium bicarbonate, 30 g of sodium borate and 30 g of biuret are uniformly mixed, 30 g of 5% dextrin water solution is added and uniformly mixed to prepare a foam drainage rod FMG02, and the result is shown in Table 3.
[ example 4 ]
The same as [ example 1 ] except that a long-chain polyamine polyether compound is used1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33SO3Na 50 g, sodium tartrate 100 g, sodium chloride 90 g and urea 30 g are mixed uniformly, and 10% cellulose water solution 30 g is added to be mixed uniformly, so as to prepare a foam drainage rod FMG03, and the results are shown in Table 4.
[ example 5 ]
(1) Preparation of foam scrubbing agent FMG 04:
a. adding 67.0 g (0.65 mol) of diethylenetriamine and 6.9 g (0.05 mol) of potassium carbonate solid into a reaction bottle provided with a mechanical stirring device, a thermometer, a dropping funnel and a normal pressure distillation device, slowly dropping 142.0 g (0.5 mol) of ethyl palmitate while stirring, reacting for 4 hours at the reaction temperature of 120-160 ℃, and collecting ethanol generated by the reaction to obtain the required amide compound C15H31CO(NHCH2CH2)2NH2The yield thereof was found to be 94.5%.
b. After removing water from a three-necked flask equipped with a reflux condenser, a dropping funnel and a thermometer, LiAlH (OEt) was added351 g (0.3 mol) and 120 ml of anhydrous ether are stirred and mixed, and 34.1 g (0.1 mol) of C is dripped into the mixture at the temperature of minus 5 to 5 DEG C15H31CO(NHCH2CH2)2NH2Adding 50 wt% anhydrous ether solution, slowly heating to about 30 deg.C, and reacting for 5 hr. Carefully pouring the reaction solution into ice water, and carrying out post-treatment to obtain a long-chain polyamine compound C15H31CH2(NHCH2CH2)2NH2The yield thereof was found to be 83.4%.
c. A pressure reactor equipped with a stirring device was charged with 130.8 g (0.4 mol) of C15H31CH2(NHCH2CH2)2NH25.2 g of potassium carbonate, 70.8 g (1.22 mol) of propylene oxide and 35.2 g (0.8 mol) of ethylene oxide are sequentially reacted at 140-160 ℃ to obtain the long-chain polyamine polyether compound2(R1=C16H33,m=2,s1+s2+2s3=3,r1+r2+2r3=2,R2=R3=R4H), yield 97.6%.
d. Long-chain polyamine polyether compounds2(R1=C16H33,m=2,s1+s2+2s3=3,r1+r2+2r3=2,R2=R3=R4H)58.9 g (0.1 mol) were mixed with 5.7 g (0.11 mol) of sodium methoxide, 13.4 g (0.11 mol of 1, 3-propanesultone and 100 ml of cyclopentanone in a four-neck flask equipped with a mechanical stirrer, a thermometer and a reflux condenser, and after the addition, the temperature was raised to reflux for 5 hours. Evaporating to remove solvent, adding ammonia water to obtain long-chain polyamine polyether compound2(R1=C16H33Ammonium propanesulfonate (R1 + R2+2R3 ═ 2, s1+ s2+2s3 ═ 3, R1+ R2+2R3 ═ 2)2、R3、R4One of them is CH2CH2CH2SO3NH4And the balance is H).
e. Long-chain polyamine polyether compound2(R1=C16H33Ammonium propanesulfonate 80g, C) with m 2, s1+ s2+2s 3-3, r1+ r2+2r 3-2)16H33OC2H4N+(CH3)2CH2COO-20 g, 100 g of potassium citrate, 60 g of urea and 60 g of biuret are uniformly mixed, 30 g of 1% polyacrylamide aqueous solution is added and uniformly mixed, and the foam drainage rod FMG04 is prepared.
(2) The same as [ example 1 ] except that the aging was carried out at 150 ℃ for 72 hours, the results are shown in Table 5.
[ example 6 ]
The same as [ example 5 ] except that in the measurement of FMG04 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid, neutral and acidic gas environments were simulated, and aging was carried out at 150 ℃ for 72 hours, and the results are shown in table 6.
[ example 7 ]
(1) Preparation of foam scrubbing agent FMG 05:
a. adding 36.0 g (0.6 mol) of ethylenediamine and 13.8 g (0.1 mol) of potassium carbonate solid into a reaction bottle provided with a mechanical stirring device, a thermometer, a dropping funnel and a normal pressure distillation device, slowly dropping 177.0 g (0.5 mol) of methyl behenate under stirring, reacting for 3 hours at the reaction temperature of 120-160 ℃, and collecting methanol generated by the reaction to obtain the required amide compound C21H43CONHCH2CH2NH2The yield thereof was found to be 91.6%.
b. Removing water from a three-neck flask device provided with a reflux condenser tube, a dropping funnel and a thermometer, adding 15.2 g (0.4 mol) of lithium aluminum hydride and 100 ml of dry dioxane, stirring, dispersing and mixing, and dropping 38.2 g (0.1 mol) of C at-10-5 DEG C21H43CONHCH2CH2NH2The 40 wt% dioxane solution is added dropwise and slowly heated to about 35 ℃ for reaction for 3 hours. Carefully pouring the reaction solution into ice water, and carrying out post-treatment to obtain a long-chain polyamine compound C21H43CH2NHCH2CH2NH2The yield thereof was found to be 87.9%.
c. A pressure reactor equipped with a stirring device was charged with 147.2 g (0.4 mol) of C21H43CH2NHCH2CH2NH25.2 g of potassium carbonate and 280.7 g (4.84 mol) of propylene oxide react at 140-160 ℃ to obtain a long-chain polyamine polyether compound3(R1=C22H45,m=1,s1+s2+s3=12,r1+r2+r3=0,R2=R3=R4H), yield 98.1%.
d. Long-chain polyamine polyether compounds3(R1=C22H45,m=1,s1+s2+s3=12,r1+r2+r3=0,R2=R3=R4H)106.4 g (0.1 mol) with 16.8 g (0.3 mol) of potassium hydroxide and 15.9 g (0.12 mol) of chloroacetic acidPotassium and 400 ml of acetone are mixed in a reaction kettle provided with a mechanical stirrer, a thermometer and a reflux condenser tube, and heated to reflux reaction for 10 hours. Evaporating the solvent to obtain the long-chain polyamine polyether compound3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK and the rest is H).
e. Long-chain polyamine polyether compound3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK, the remainder H)15 g, C22H45OC2H4N+(CH2CH2OH)2(CH3)CH2COO-90 g internal olefin sulfonate IOS (C)19~23)30 g, 100 g of sodium sulfate, 100 g of sodium tartrate and 70 g of potassium chloride are mixed uniformly, 60 g of 10% polyethylene glycol is added and mixed uniformly, and the foam drainage rod FMG05 is prepared.
(2) The same as [ example 1 ] except that the aging was carried out at 200 ℃ for 24 hours, the results are shown in Table 7.
[ example 8 ]
The same as [ example 7 ] except that in the measurement of FMG05 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid, neutral and acidic gas environments were simulated, and aging was performed at 200 ℃ for 24 hours, and the results are shown in table 8.
[ example 9 ]
(1) Preparation of foam scrubbing agent FMG 06:
a. adding 36.0 g (0.6 mol) of ethylenediamine and 13.8 g (0.1 mol) of potassium carbonate solid into a reaction bottle provided with a mechanical stirring device, a thermometer, a dropping funnel and a normal pressure distillation device, slowly dropping 158.3 g (0.5 mol) of methyl abietate (formula 3) while stirring, reacting at the reaction temperature of 120-160 ℃ for 8 hours, and collecting methanol generated by the reaction to obtain the required amide compound C19H29CONHCH2CH2NH2The yield thereof was found to be 85.6%.
Figure BDA0001437255110000121
b. Removing water from a three-neck flask device provided with a reflux condenser tube, a dropping funnel and a thermometer, adding 13.3 g (0.35 mol) of lithium aluminum hydride and 100 ml of dry dioxane, stirring, dispersing and mixing, and dropping 34.4 g (0.1 mol) of C at-10-5 DEG C19H29CONHCH2CH2NH2The 40 wt% dioxane solution is added dropwise and slowly heated to about 35 ℃ for reaction for 5 hours. Carefully pouring the reaction liquid into ice water, and carrying out post-treatment to obtain a rosin polyamine compound C19H29CH2NHCH2CH2NH2The yield thereof was found to be 73.2%.
c. To a pressure reactor equipped with a stirring device was added 132.0 g (0.4 mol) of C19H29CH2NHCH2CH2NH25.0 g of potassium hydroxide and 160.2 g (3.64 mol) of ethylene oxide react at 140-160 ℃ to obtain the rosin polyamine polyether compound4(R1=C20H31,m=1,s1+s2+s3=0,r1+r2+r3=9,R2=R3=R4H), yield 91.4%.
d. Rosin polyamine polyether compounds4(R1=C20H31,m=1,s1+s2+s3=0,r1+r2+r3=9,R2=R3=R4H)72.6 g (0.1 mol) were mixed with 8.0 g (0.2 mol) of sodium hydroxide, 33.3 g (0.2 mol) of sodium 2-chloroethanesulfonate and 100 ml of toluene in a reaction vessel equipped with a mechanical stirrer, a thermometer and a reflux condenser and heated to reflux for 6 hours. Evaporating the solvent to obtain the long-chain polyamine polyether compound4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, remainder H).
e. Long-chain polyamine polyether compound4(R1=C20H31,m=1,s1+s2+s3=0,r1+r2Sodium ethanesulfonate (R) of + R3 ═ 9)2、R3、R4One of them is CH2CH2SO3Na, the rest is H)90 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g of potassium phthalate, 50 g of potassium phthalate, 150 g of biuret and 30 g of 5 percent polyethylene glycol solution are added and mixed evenly to prepare the foam drainage rod FMG 06.
(2) The results are shown in Table 9, as in example 1.
[ example 10 ]
The same as [ example 9 ] except that in the measurement of FMG06 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid to simulate neutral and acid gas-containing environments, and the results are shown in table 10.
[ example 11 ]
The same as [ example 10 ] except that a long-chain polyamine polyether compound is used4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the rest is H)30 g, C16H33C6H4SO390 g of Na (hexadecyl sodium benzene sulfonate), 30 g of potassium citrate, 50 g of urea, 100 g of potassium carbonate and 60 g of sodium acetate are uniformly mixed, 30 g of 1% polyacrylamide aqueous solution is added and uniformly mixed to prepare a foam drainage rod FMG07, and the result is shown in Table 11.
[ COMPARATIVE EXAMPLE 1 ]
The same as [ example 1 ] except that the long-chain polyamine polyether compounds are used1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)100 g, C16H33OC2H4N+(CH3)3Br-100 g, C16H33SO3K100 g substituted long-chain polyamine polyether compound1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g ", other additives were unchanged to form foam drainage sticks FMG08, FMG09, and FMG10, with simulated water of 100,000mg/LNaCl, the results are shown in table 12.
[ COMPARATIVE EXAMPLE 2 ]
The same as [ example 5 ] except that the long-chain polyamine polyether compounds are used2(R1=C16H33100 g of ammonium propanesulfonate with m ═ 2, s1+ s2+2s3 ═ 3, r1+ r2+2r3 ═ 2), and C16H33OC2H4N+(CH3)2CH2COO-100 g of substituted long-chain polyamine polyether compound2(R1=C16H33Ammonium propanesulfonate 80g, C) with m 2, s1+ s2+2s 3-3, r1+ r2+2r 3-2)16H33OC2H4N+(CH3)2CH2COO-20 grams ", other additives were unchanged to form foam drainage sticks FMG11 and FMG12 with simulated water at 100,000mg/LNaCl, and the results are shown in Table 13.
[ COMPARATIVE EXAMPLE 3 ]
The same as [ example 7 ] except that the long-chain polyamine polyether compound is used3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK, the remainder H)135 g of a substituted long-chain polyamine polyether compound3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK, the remainder H)15 g, C22H45OC2H4N+(CH2CH2OH)2(CH3)CH2COO-90 g internal olefin sulfonate IOS (C)19~23)30 g "of other additives, forming a foam drainage bar FMG13 with simulated water of 100,000mg/LNaCl, the results are shown in Table 13.
[ COMPARATIVE EXAMPLE 4 ]
The same as [ example 9 ] except that the long-chain polyamine polyether compound is used4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the remainder being H)100 g of substituted long-chain polyamine polyether compound4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the rest is H)90 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g ", other additives were unchanged to form a foam drainage stick FMG14 with simulated water at 100,000mg/LNaCl, the results are shown in Table 13.
[ COMPARATIVE EXAMPLE 5 ]
The same as [ example 1 ], except that "C" is used17H33CO(NHCH2CH2)5NH250 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g of "substituted" long-chain polyamine polyether Compound 1 (R)1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g ", other additives were unchanged to form a foam drainage stick FMG15 with simulated water of 100,000mg/LNaCl, the results are shown in Table 14.
[ COMPARATIVE EXAMPLE 6 ]
The same as [ comparative example 5 ] except that in measuring the FMG15 performance, pH was adjusted to 7 and 4 with hydrochloric acid to simulate neutral and acidic gas environments, and the results are shown in table 15.
[ COMPARATIVE EXAMPLE 7 ]
The same as [ example 9 ], except that "C" is used19H29CONHCH2CH2NH290 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g of a substituted long-chain polyamine polyether compound4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the rest is H)90 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g ", other additives were unchanged to form a foam drainage stick FMG16 with simulated water at 100,000mg/LNaCl, the results are shown in Table 14.
[ COMPARATIVE EXAMPLE 8 ]
The same as in comparative example 7, except that the pH was adjusted to 2 with hydrochloric acid to simulate a high acid-containing gas atmosphere when measuring the FMG16 performance, the results are shown in table 15.
TABLE 1
Figure BDA0001437255110000161
TABLE 2
Figure BDA0001437255110000162
TABLE 3
Figure BDA0001437255110000171
TABLE 4
Figure BDA0001437255110000172
TABLE 5
Figure BDA0001437255110000181
TABLE 6
Figure BDA0001437255110000182
TABLE 7
Figure BDA0001437255110000191
TABLE 8
Figure BDA0001437255110000192
TABLE 9
Figure BDA0001437255110000201
Watch 10
Figure BDA0001437255110000202
TABLE 11
Figure BDA0001437255110000211
TABLE 12
Figure BDA0001437255110000212
Watch 13
Figure BDA0001437255110000221
TABLE 14
Figure BDA0001437255110000222
Watch 15
Figure BDA0001437255110000223

Claims (9)

1. The solid foam drainage agent composition comprises the following components in parts by weight:
(1)1 part of polyamine polyether compound;
(2) 0.1-10 parts of cosurfactant;
(3) 0.1-200 parts of solid filler;
(4) 0.01-0.1 parts of adhesive;
wherein the polyamine polyether compound has a general molecular formula shown in formula (1):
Figure FDA0003048519520000011
in the formula (1), R1Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R2、R3、R4Independently selected from H, C1~C5Hydrocarbyl or substituted hydrocarbyl carboxylates, C1~C5Alkyl or substituted alkyl sulfonates, C1~C5Hydrocarbyl or substituted hydrocarbyl phosphates or C1~C5At least one of alkyl sulfate or substituted alkyl sulfate, which is not H at the same time; m is-N (A) CH2CH2-the number of fragments, m ═ 1 to 10; a is a substituent represented by the formula (4); s1, s2 and s3 are the addition number of propoxy groups PO, s1 is 0-30, s2 is 0-30, and s3 is 0-30; r1, r2 and r3 are the addition number of ethoxy EO, r1 is 0-30, r2 is 0-30, r3 is 0-30, and s1+ s2+ m s3 and r1+ r2+ m r3 are not zero at the same time;
Figure FDA0003048519520000012
the cosurfactant is at least one of a zwitterionic surfactant, a cationic surfactant and an anionic surfactant; the zwitterionic or cationic surfactant has a general molecular formula shown in formula (2):
Figure FDA0003048519520000013
in the formula (2), R5Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R6、R7Independently selected from (CH)2)aOH、(CH2)bCH3Or C6H5CH2One of (1), R8Is selected from (CH)2)aOH、(CH2)bCH3、C6H5CH2、(CH2)c、(CH2)c(CHOH)d(CH2)eWherein a is any integer from 2 to 4, b is any integer from 0 to 5, c is any integer from 1 to 4, d is any integer from 0 to 3, and e is any integer from 1 to 4; n is the addition number of propoxy groups PO, and n is 0-15; p is an ethoxy groupThe addition number of EO, p is 0-30; x-Is selected from OH-Halogen anion, HCO3-、NO3 -、CH3OSO3 -、CH3COO-、COO-、SO3 -Or OSO3 -One of (1);
the anionic surfactant has a general molecular formula shown in formula (3):
Figure FDA0003048519520000021
in the formula (3), R9And R10The sum is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, M is selected from hydrogen, alkali metal or of the formula NR11(R12)(R13)(R14) At least one of the groups shown, R11、R12、R13、R14Is independently selected from H, (CH)2)aOH or (CH)2)bCH3Wherein a is any integer of 2-4, and b is any integer of 0-5.
2. The solid foam drainage agent composition of claim 1, wherein R is1、R5Is C8~C24Hydrocarbyl or substituted hydrocarbyl; r9And R10The sum of C7~C23Hydrocarbyl or substituted hydrocarbyl; r2、R3、R4Is H, CH2COOM1、(CH2)3SO3M1Or CH2(CHOH)CH2SO3M1And is not simultaneously H; r6、R7Is CH3、C2H5、(CH2)2OH or C6H5CH2One of (1); r8Is CH3、C2H5、(CH2)2OH or C6H5CH2Or R is8X-Is CH2COO-、(CH2)3SO3 -、CH2(CHOH)CH2SO3 -One of (1); m is 1-5; s1+ s2+ m s3 is 0-5, r1+ r2+ m r3 is 0-10, and is not zero at the same time; n is 0 to 5, and p is 0 to 5.
3. The solid foam drainage agent composition of claim 2, wherein the M is1Is hydrogen, an alkali metal or of the formula NR11(R12)(R13)(R14) At least one of the groups shown, R11、R12、R13、R14Is independently selected from H, (CH)2)aOH or (CH)2)bCH3Wherein a is any integer of 2-4, and b is any integer of 0-5.
4. The solid foam drainage agent composition of claim 1, wherein the solid filler is at least one of carbonate, bicarbonate, sulfate, phosphate, borate, metal halide, formate, acetate, tartaric acid and salts, citric acid and salts, phthalic acid and salts, gallic acid and salts, urea, biuret; the adhesive is at least one of dextrin, epoxy resin, polyacrylamide, starch, cellulose and polyethylene glycol.
5. The solid foam drainage agent composition of claim 4, wherein the solid filler is 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, biuret; the adhesive is at least one of polyacrylamide, starch and polyethylene glycol.
6. A method of making the solid foam drainage agent composition of any of claims 1 to 5, comprising the steps of:
(1) preparation of polyamine polyether compounds
a. Amidation reaction:
r is to be0COOR' and H (NHCH)2CH2)mNH2Mixing the catalysts according to the molar ratio of 1 (1-2) to 0-0.5, reacting for 3-15 hours at the reaction temperature of 50-200 ℃ under stirring, and evaporating alcohol or water generated in the reaction under normal pressure or reduced pressure to obtain the required amide compound R0CO(NHCH2CH2)mNH2(ii) a Wherein R is0Is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, R' is selected from H and C1~C8M is 1-10, and the catalyst is at least one selected from alkali metal hydroxide, alkali metal alkoxide and alkali metal carbonate;
b. reduction reaction:
R0CO(NHCH2CH2)mNH2the reduction of the lactam adopts a catalytic hydrogenation method, and generates heterogeneous catalytic reaction at high temperature and high pressure to generate corresponding amine, or adopts the following steps: the R synthesized in the step a0CO(NHCH2CH2)mNH2And H-Y+Reduction in an aprotic solvent to give R0CH2(NHCH2CH2)mNH2(ii) a Wherein H-Y+Is a metal compound, a metal alkyl compound, a metal amino compound;
c. and (3) polyether esterification:
in the presence of a basic catalyst, the R synthesized in the step b0CH2(NHCH2CH2)mNH2Sequentially reacting with required amount of propylene oxide and ethylene oxide to obtain long-chain polyamine polyether intermediate product R0CH2{N[(CHCH3CH2O)s3(CH2CH2O)r3H][CH2CH2]}mN[(CHCH3CH2O)s1(CH2CH2O)r1H][CHCH3CH2O)s2(CH2CH2O)r2)H];
d. Carboxylation or sulfonation reaction:
c, mixing the long-chain polyamine polyether intermediate product obtained in the step c with an ionizing agent and a base in a molar ratio of 1: (1-5): (1-10) reacting in a solvent at 50-120 ℃ for 3-20 hours to generate polyamine polyether carboxylate or polyamine polyether sulfonate shown in the structural formula (1); the ionizing agent is selected from XR15Y1Or XR'15Y′1At least one of; the base is selected from alkali metal hydroxide or alkali metal alkoxide; the XR15Y1Or XR'15Y′1Selected from alkali metal salts of chloroacetic acid, bromoacetic acid, 3-chloro-2-hydroxypropanesulfonic acid, and 2-chloroethanesulfonic acid;
(2) uniformly mixing the polyamine polyether compound synthesized in the step (1), the cosurfactant, the solid filler and the adhesive according to the required parts by mass, and then pressing and forming to prepare the solid foam drainage agent composition.
7. The method of making a solid foam drainage agent composition of claim 6, wherein R is the same as R in step a0COOR’、H(NHCH2CH2)mNH2The molar ratio of the catalyst is (1-1.3) to (0-0.1), and the catalyst is at least one of sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate; step b said H-Y+Is LiAlH4Or NaBH4Wherein the aprotic solvent is at least one of diethyl ether, tetrahydrofuran and dioxane.
8. The method of making a solid foam drainage agent composition of claim 6, wherein the long-chain polyamine polyether intermediate of step d: ionizing agent: the molar ratio of the alkali is 1 to (1-2) to (1-4, and the solvent is selected from C3~C8Ketone and C6~C9At least one aromatic hydrocarbon of (1).
9. The use of the solid foam drainage agent composition of any one of claims 1 to 5 in drainage and gas production of acidic high-temperature high-salinity ultra-deep gas wells.
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