CN104974730B - A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity - Google Patents

A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity Download PDF

Info

Publication number
CN104974730B
CN104974730B CN201510321512.2A CN201510321512A CN104974730B CN 104974730 B CN104974730 B CN 104974730B CN 201510321512 A CN201510321512 A CN 201510321512A CN 104974730 B CN104974730 B CN 104974730B
Authority
CN
China
Prior art keywords
foam discharging
discharging agent
surfactant
water
cationic
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510321512.2A
Other languages
Chinese (zh)
Other versions
CN104974730A (en
Inventor
武俊文
熊春明
雷群
张建军
曹光强
李隽�
李楠
王云
贾敏
刘岩
何春艳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Natural Gas Co Ltd
Original Assignee
China Petroleum and Natural Gas Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by China Petroleum and Natural Gas Co Ltd filed Critical China Petroleum and Natural Gas Co Ltd
Priority to CN201510321512.2A priority Critical patent/CN104974730B/en
Publication of CN104974730A publication Critical patent/CN104974730A/en
Application granted granted Critical
Publication of CN104974730B publication Critical patent/CN104974730B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • 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
    • 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
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mining & Mineral Resources (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Fluid Mechanics (AREA)
  • Physics & Mathematics (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Environmental & Geological Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

The present invention provides a kind of high temperature resistance, the foam discharging agents and the preparation method and application thereof of high salinity.By percentage to the quality, which includes 15 40% anion surfactants, 5 15% cationic surfactants, and surplus is deionized water;Wherein:The anion surfactant includes fatty alcohol polyoxyethylene ether sulfate, α sodium olefin sulfonates or lauryl sodium sulfate;The cationic surfactant includes Cationic Gemini Surfactant.The present invention also provides the methods for preparing above-mentioned foam discharging agent:Anion surfactant and cationic surfactant are added at one time in reaction vessel, deionized water is added, obtains mixed solution;Above-mentioned mixed solution is heated to 50 60 DEG C, stirring obtains foam discharging agent.Foam discharging agent provided by the invention can solve the problem of the foaming properties rapid drawdown when temperature and salinity increase of existing foam discharging agent, can be used for the water drainage-gas recovery technology of deep layer high temperature, high salinity gas well.

Description

A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity
Technical field
The present invention relates to a kind of high temperature resistance, the foam discharging agents and the preparation method and application thereof of high salinity, and it is natural to belong to oil Gas exploits field.
Background technology
With going deep into for gas field development, most gas fields have been enter into the middle and later periods of exploitation, since strata pressure constantly declines, lead Edge water propelling and bottom water is caused to rise, gas well water breakthrough Hou Bowl mouth rapid pressure drops, since fluid-carrying capability decline causes shaft bottom hydrops, It will lead to the Qi Bowl underproduction even stop-spraying.For this present situation, it is necessary to carry out drainage gas recovery in time, solve gas well drain and ask Topic.Wherein, with its effect, the reasons such as good, easy for construction and relatively inexpensive become water drainage-gas recovery technology to foam drainage gas recovery technique It is preferred.Foam drainage gas recovery technique is by injecting in the insufficient producing well of fluid-carrying capability, being allowed to and shaft bottom hydrops by foam discharging agent The resistance aqueous foam that a large amount of low-density are mixed and generated under the agitation of air-flow is carried to ground from shaft bottom with air-flow, improves gas well Fluid-carrying capability, to achieve the purpose that volume increase, stable yields and extend its flush stage.The performance of foam discharging agent is adopted as foaming water discharge The key of gas technology, i.e., under certain external condition such as temperature, salinity, foam discharging agent should have higher foamability, steady Bubble ability and fluid-carrying capability.
Domestic existing foam discharging agent applies in general to 90 DEG C or less and salinity is less than the stratum of 100000ppm, with The raising of temperature and salinity, foamability and stability substantially reduce, and part foam discharging agent does not rise even when higher than 120 DEG C Bubble, to hinder application of the foam drainage gas recovery technique in high temperature, high salinity water-producing gas well.The main component of foam discharging agent It is surfactant, at present for the research of foam discharging agent mainly by being compounded between Surfactant, however, these Compounding is mostly focused between anion surfactant and anion surfactant, anion surfactant and both sexes from Between sub- surfactant, and for the very understatement of the research between anion surfactant and cationic surfactant Road.
Invention content
In order to solve the above technical problems, the purpose of the present invention is to provide a kind of foam discharging agent, the foam discharging agent is in temperature range Under conditions of being 50000-250000ppm for 100-160 DEG C, salinity, there is higher initial bubbles volume V0, half foam life period t1/2And liquid rate is taken, it can solve the problems, such as the water pumping gas production of high temperature, high salinity water-producing gas well.
In order to achieve the above objectives, the present invention provides a kind of foam discharging agents, and by percentage to the quality, which includes 15- 40% anion surfactant, 5-15% cationic surfactants, surplus are deionized water;Wherein:
The anion surfactant includes fatty alcohol polyoxyethylene ether sulfate, α-sodium olefin sulfonate or dodecyl Sodium sulphate;
The cationic surfactant includes Cationic Gemini Surfactant.
Research in the prior art between anion surfactant and cationic surfactant is fresh few, this is because Anion surfactant is easy to generate precipitation when compounding with cationic surfactant, cannot be answered to lose effectiveness With but the present invention creatively compounds anion surfactant and cationic surfactant, makes between the two Special synergistic effect is generated, in the microcosmic upper good position adaptability of generation, special synergistic effect is generated, enhances vacuolar membrane Compactness significantly enhances the performance of foam discharging agent.
In above-mentioned foam discharging agent, it is preferable that the fatty alcohol polyoxyethylene ether sulfate includes fatty alcohol polyoxyethylene ether Sodium sulphate (AES), AES have preferable foaming characteristic and water solubility.
In above-mentioned foam discharging agent, it is preferable that the molecular structure of the Cationic Gemini Surfactant is
In formula, m=12-18.
There is Cationic Gemini Surfactant provided by the invention pectinate texture, such special construction to be conducive to it Finer and close arrangement is formed in gas-liquid interface, can effectively prevent the coalescence and disproportionation of bubble, it is steady to reach enhancing foam Qualitative effect.
The present invention also provides a kind of methods preparing above-mentioned foam discharging agent comprising following steps:
Anion surfactant and cationic surfactant are added at one time in reaction vessel, then be added go from Sub- water, obtains mixed solution;
Above-mentioned mixed solution is heated to 50-60 DEG C, stirring obtains foam discharging agent.
In the above-mentioned methods, it is preferable that the cationic surfactant is prepared by following steps:
2-2.5g alkyl dimethyls ammonium bromide and excessive 1,2- Bromofumes are dissolved in 50-70mL absolute ethyl alcohols, in 50- Flow back 36-48h at 80 DEG C, obtains mixture;Said mixture is evaporated at 37 DEG C, obtains cationic surfactant;More Preferably, the dosage of 1, the 2- Bromofumes is 4-8mL.
In the above-mentioned methods, it is preferable that the alkyl carbon number in the alkyl dimethyl ammonium bromide is C12-C18.
In the above-mentioned methods, it is preferable that the mixing speed is 200-400r/min, mixing time 20-25min.
Foam discharging agent provided by the invention can be applied in water-producing gas well water pumping gas production.
In above application, it is preferable that the temperature of mineralized water is 100-160 DEG C in the water-producing gas well.
In above application, it is preferable that the salinity of mineralized water is 50000-250000ppm in the water-producing gas well.
Beneficial effects of the present invention:
1) technical solution provided by the invention creatively by anion surfactant and cationic surfactant into Row compounding, makes to produce special synergistic effect between the two, significantly enhances the performance of foam discharging agent;
2) foam discharging agent provided by the invention is in the condition that temperature is 100-160 DEG C, salinity is 50000-250000ppm Under, there is higher initial bubbles volume V0, half foam life period t1/2And take liquid rate;Existing foam discharging agent can be solved in temperature and mine When change degree increases, the problem of foaming properties rapid drawdown, it can be used for the water drainage-gas recovery technology of deep layer high temperature, high salinity gas well;
3) foam discharging agent composition provided by the invention is simple, and it is convenient to prepare, cheap, nontoxic low irritant.
Specific implementation mode
In order to which technical characteristic, purpose and the advantageous effect to the present invention are more clearly understood, now to the skill of the present invention Art scheme carry out it is described further below, but should not be understood as to the present invention can practical range restriction.
Embodiment 1
Present embodiments provide a kind of high temperature resistance, high salinity foam discharging agent and preparation method thereof.The preparation method includes Following steps:
1) Gemini cationic surfactants are prepared
Respectively by 2g Dodecydimethylammonium bronides, dodecyldimethylamine base ammonium bromide, hexadecyldimethyl benzyl ammonium bromination Ammonium, octadecyldimethyl ammonium bromide are dissolved in absolute ethyl alcohol with 4mL glycol dibromides (excessive to ensure to react abundant completion) In (50mL), flow back 48h at 80 DEG C or so.Mixture after reaction is spin-dried on Rotary Evaporators 37 DEG C, respectively obtains m =12,14,16,18 Gemini cationic surfactants;The structure of the Gemini cationic surfactants such as I institute of formula Show
Wherein, Gemini cationic surfactants are positive by the Gemini of above-mentioned m=12,14,16,18 in the present embodiment Ionic surface active agent is 1 according to mass ratio:1:3:Made of 1 mixes;
2) foam discharging agent is prepared
By percentage to the quality, the raw material composition of foam discharging agent includes in the present embodiment:25% fatty alcohol polyoxyethylene ether sulphur Hydrochlorate (AES), 8%Gemini cationic surfactants, surplus are deionized water;
According to above-mentioned dosage, sodium sulfate of polyethenoxy ether of fatty alcohol and Gemini cationic surfactants are disposably added Enter in stainless steel cauldron, add deionized water, this mixed solution is heated to 55 DEG C, is stirred at 200-400r/min 20min obtains foam discharging agent GWJ-1.
Embodiment 2
The present embodiment provides the foam discharging agents and preparation method thereof for having given a kind of high temperature resistance, high salinity.The preparation method packet Include following steps:
1) Gemini cationic surfactants are prepared
Respectively by 2g Dodecydimethylammonium bronides, dodecyldimethylamine base ammonium bromide, hexadecyldimethyl benzyl ammonium bromination Ammonium, octadecyldimethyl ammonium bromide are dissolved in absolute ethyl alcohol with 4mL glycol dibromides (excessive to ensure to react abundant completion) In (50mL), flow back 48h at 80 DEG C or so.Mixture after reaction is spin-dried on Rotary Evaporators 37 DEG C, respectively obtains m =12,14,16,18 Gemini cationic surfactants;The structure of the Gemini cationic surfactants such as I institute of formula Show
Wherein, Gemini cationic surfactants are positive by the Gemini of above-mentioned m=12,14,16,18 in the present embodiment Ionic surface active agent is 1 according to mass ratio:1:3:1 mixes;
2) foam discharging agent is prepared
By percentage to the quality, the raw material composition of foam discharging agent includes in the present embodiment:35% fatty alcohol polyoxyethylene ether sulphur Hydrochlorate (AES), 13%Gemini cationic surfactants, surplus are deionized water;
According to above-mentioned dosage, sodium sulfate of polyethenoxy ether of fatty alcohol and Gemini cationic surfactants are disposably added Enter in stainless steel cauldron, add deionized water, this mixed solution is heated to 55 DEG C, is stirred at 200-400r/min 20min obtains foam discharging agent GWJ-2.
Embodiment 3
The foam discharging agent GWJ-1 that the present embodiment is provided for above-described embodiment 1 is first under the conditions of different temperatures and salinity Beginning foaming volume V0, half foam life period t1/2And throughput when being 5L/min the liquid carry over of 15min be tested, and in phase It is compared with the performance with certain domestic commercially available foam discharging agent 1 and 2 under test condition.
Instrument used in test process is that (the high temperature and pressure foam evaluations instrument is the patent No. to high temperature and pressure foam evaluations instrument High temperature and pressure foam evaluations instrument recorded in the utility model patent of ZL201120400940.1, notification number CN202228059U); The mineralized water of test is after being analyzed according to the water of live natural gas well output, using NaCl, CaCl2、MgCl2、KCl、 Na2SO4、NaHCO3It is prepared.
It is described that the specific test method is as follows:
1) foaming characteristic of foam discharging agent is tested with foam stability:
A, temperature in evaluating apparatus is first risen into nominative testing temperature;
B, the foam discharging agent solution that 200mL mass concentrations are 3% (by the densimeter of surfactant) is pumped into evaluation dress again It sets;
C, pressure rises to 1MPa (nitrogen), records initial bubbles volume and half foam life period.
2) fluidity of taking of foam discharging agent is tested:
A, temperature in evaluating apparatus is first risen into nominative testing temperature;
B, the foam discharging agent solution that 200mL mass concentrations are 3% (by the densimeter of surfactant) is pumped into evaluation dress again It sets;
C, nitrogen is pumped into the speed of 5L/min in evaluating apparatus, collects and record the liquid carry over of 15min.
Table 1:The performance (salinity 250000ppm) of foam discharging agent (GWJ-1) under different temperatures
Table 2:The performance (salinity 250000ppm) of certain domestic commercially available foam discharging agent 1
Table 3:The performance (salinity 250000ppm) of certain domestic commercially available foam discharging agent 2
Table 4:The performance of foam discharging agent (GWJ-1) under different salinities (temperature is 130 DEG C)
Table 5:The performance of certain domestic commercially available foam discharging agent 1 (temperature is 130 DEG C)
Table 6:The performance of certain domestic commercially available foam discharging agent 2 (temperature is 130 DEG C)
Specific test result is as shown in table 1-6, wherein table 1 and the foam discharging agent GWJ-1 that respectively embodiment 1 provides of table 4 exist The performance test results under the conditions of different temperatures and salinity;Table 2 and 5 is respectively certain domestic commercially available foam discharging agent 1 in different temperatures With the performance test results under the conditions of salinity;Table 3 and 6 is respectively certain domestic commercially available foam discharging agent 2 in different temperatures and salinity Under the conditions of the performance test results;The above-mentioned country's certain commercially available foam discharging agent 1 and 2 is provided by Chengdu Fuji Science and Technology Co., Ltd. 's.
Foam discharging agent provided by the invention is can be seen that temperature is 100-160 DEG C, salinity is from above-mentioned test result There is higher foaming characteristic, foam stability within the scope of 50000-250000ppm and take liquid rate.

Claims (6)

1. a kind of foam discharging agent, by percentage to the quality, the foam discharging agent include 15-40% anion surfactants, 5-15% sun Ionic surface active agent, surplus are deionized water;Wherein:
The anion surfactant is fatty alcohol polyoxyethylene ether sulfate;The fatty alcohol polyoxyethylene ether sulfate packet Include sodium sulfate of polyethenoxy ether of fatty alcohol;
The cationic surfactant includes Cationic Gemini Surfactant;The Cationic Gemini Surfactant Molecular structure be
And the Gemini cationic surfactants by m=12,14,16,18 Gemini cationic surfactants according to Mass ratio is 1:1:3:1 mixes.
2. a kind of method preparing foam discharging agent described in claim 1 comprising following steps:
Anion surfactant and cationic surfactant are added at one time in reaction vessel, deionization is then added Water obtains mixed solution;
Above-mentioned mixed solution is heated to 50-60 DEG C, stirring obtains foam discharging agent.
3. according to the method described in claim 2, wherein:The speed of the stirring is 200-400r/min, and the time of stirring is 20-25min。
4. application of the foam discharging agent described in claim 1 in water-producing gas well water pumping gas production.
5. application according to claim 4, wherein:The temperature of mineralized water is 100-160 DEG C in the water-producing gas well.
6. application according to claim 4 or 5, wherein:The salinity of mineralized water is 50000- in the water-producing gas well 250000ppm。
CN201510321512.2A 2015-06-12 2015-06-12 A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity Active CN104974730B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510321512.2A CN104974730B (en) 2015-06-12 2015-06-12 A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510321512.2A CN104974730B (en) 2015-06-12 2015-06-12 A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity

Publications (2)

Publication Number Publication Date
CN104974730A CN104974730A (en) 2015-10-14
CN104974730B true CN104974730B (en) 2018-09-04

Family

ID=54271706

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510321512.2A Active CN104974730B (en) 2015-06-12 2015-06-12 A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity

Country Status (1)

Country Link
CN (1) CN104974730B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105199701B (en) * 2015-10-21 2018-10-02 西安长庆化工集团有限公司 The foam discharging agent and preparation method thereof of high temperature resistance, anti-high salinity and condensate oil
CN105199702B (en) * 2015-10-21 2018-07-06 西安长庆化工集团有限公司 A kind of foam discharging agent and preparation method thereof of condensate oil, methanol
CN108251091A (en) * 2016-12-29 2018-07-06 中国石油天然气股份有限公司 A kind of anti-salinity, condensate oil fluid foaming agent and preparation method thereof
CN107400505B (en) * 2017-07-06 2020-11-24 中国石油天然气股份有限公司 High-temperature solid foam scrubbing agent and preparation method thereof
CN109679621B (en) * 2017-10-18 2021-05-11 中国石油化工股份有限公司 High-temperature-resistant high-salt solid foam drainage agent, and preparation method and application thereof
CN109679608B (en) * 2017-10-18 2021-02-09 中国石油化工股份有限公司 High-temperature-resistant acid-resistant foam drainage agent, preparation method and application
CN109679607B (en) * 2017-10-18 2021-05-11 中国石油化工股份有限公司 Method for water drainage and gas production by adopting high-temperature-resistant high-salt foam drainage agent
CN109679614B (en) * 2017-10-18 2021-05-11 中国石油化工股份有限公司 Method for water drainage and gas recovery by adopting high-temperature-resistant acid-resistant solid foam drainage agent
CN110317588A (en) * 2018-03-29 2019-10-11 中国石油化工股份有限公司 A kind of cationic surfactant and preparation method thereof and foaming agent and its application
CN114163986A (en) * 2021-12-16 2022-03-11 夏中华 Sterilization foam drainage agent for oil and gas fields and manufacturing device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1564861A (en) * 2001-08-03 2005-01-12 Lg生活健康株式会社 Complexed surfactant system
CN102212344A (en) * 2011-04-08 2011-10-12 西安石油大学 High-temperature foam scrubbing agent for drainage gas recovery
CN102744005A (en) * 2012-07-13 2012-10-24 福州大学 Foam stabilizer based on Gemini surfactant
CN104140802A (en) * 2013-10-29 2014-11-12 中国石油化工股份有限公司 Foam drainage agent for gas well drainage gas recovery

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1564861A (en) * 2001-08-03 2005-01-12 Lg生活健康株式会社 Complexed surfactant system
CN102212344A (en) * 2011-04-08 2011-10-12 西安石油大学 High-temperature foam scrubbing agent for drainage gas recovery
CN102744005A (en) * 2012-07-13 2012-10-24 福州大学 Foam stabilizer based on Gemini surfactant
CN104140802A (en) * 2013-10-29 2014-11-12 中国石油化工股份有限公司 Foam drainage agent for gas well drainage gas recovery

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
季铵盐gemini表面活性剂与SDS的相互作用-相行为、胶团化及流变特性;李修芝;《中国优秀博硕士学位论文全文数据库 (硕士) 工程科技Ⅰ辑》;20040315;第B014-308页 *

Also Published As

Publication number Publication date
CN104974730A (en) 2015-10-14

Similar Documents

Publication Publication Date Title
CN104974730B (en) A kind of foam discharging agent and the preparation method and application thereof of high temperature resistance, high salinity
CN104893702B (en) One kind is used to contain H2The foam discharging agent of the water-producing gas well water pumping gas production of S gases
CN105086980B (en) A kind of foam discharging agent for deep gas well water pumping gas production and preparation method thereof
CN104531121B (en) A kind of methanol tolerance, condensate oil, the foaming water discharge agent of anti-high salinity
CN106244127B (en) A kind of environment-friendly type foaming water discharge agent and preparation method thereof
CN103642481B (en) Heat-resistant salt-resistant type low interfacial tension foam flooding finish and preparation method thereof
CN103059826B (en) Foam water-drainage agent and its aqueous solution
CN104342096B (en) A kind of slow release type foaming agent
CN105154055B (en) A kind of ultralow interfacial tension foam flooding system and its application method
CN102977872B (en) A kind of strengthening foam oil-displacing agent for enhancing crude oil recovery efficiency in tertiary recovery and preparation method thereof
CN104498016B (en) Foam agent used in carbon-dioxide flooding and preparation method of foam agent
CN103881683A (en) Foaming agent for plugging gas channeling in displacement of reservoir oil by using CO2
CN107880865A (en) A kind of low interfacial tension foam flooding finish and preparation method thereof
CN105199700A (en) Oligomeric betanine type foam drainage agent and preparation method
CN108929668A (en) Resistance to foaming agent with high salt of one kind and preparation method thereof
CN107573917A (en) Solid foam water discharge agent composition and its preparation method and application
CN107603581A (en) Efficient foam water discharge agent composition and its preparation method and application
CN105062453A (en) Solid foam water draining agent for gas field and preparation method thereof
CN103553421A (en) Environment-friendly compound concrete foaming agent and preparation method thereof
CN111039819A (en) Temperature-resistant salt-tolerant viscoelastic surfactant and preparation method and application thereof
CN104109524B (en) Reinforced foam flooding composition for high salinity reservoirs, and preparation method thereof
CN111088019B (en) Reinforced high-temperature-resistant foam drainage agent composition, preparation method thereof and gas production method
CN103013477B (en) Under-balanced drilling high temperature stiff foam and preparation method thereof
CN107794031B (en) Nitrogen foam fracturing fluid system suitable for low-pressure lean water-containing coal bed gas well
CN108997994A (en) A kind of oil field anti-channeling displacement of reservoir oil foaming agent and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant