CN107652951A - Preparation method of polyamide inhibitor for drilling fluid - Google Patents

Preparation method of polyamide inhibitor for drilling fluid Download PDF

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Publication number
CN107652951A
CN107652951A CN201711076418.0A CN201711076418A CN107652951A CN 107652951 A CN107652951 A CN 107652951A CN 201711076418 A CN201711076418 A CN 201711076418A CN 107652951 A CN107652951 A CN 107652951A
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China
Prior art keywords
substance
drilling fluid
preparation
polyamides amine
heating
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CN201711076418.0A
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Chinese (zh)
Inventor
袁志平
陶怀志
李巍
王参书
刘伟
刘滨
王睿
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CNPC Chuanqing Drilling Engineering Co Ltd
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CNPC Chuanqing Drilling Engineering Co Ltd
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Priority to CN201711076418.0A priority Critical patent/CN107652951A/en
Publication of CN107652951A publication Critical patent/CN107652951A/en
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    • 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
    • C09K8/02Well-drilling compositions
    • C09K8/03Specific additives for general use in well-drilling compositions
    • C09K8/035Organic additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • C08G69/28Preparatory processes
    • 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
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/12Swell inhibition, i.e. using additives to drilling or well treatment fluids for inhibiting clay or shale swelling or disintegrating

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Polyamides (AREA)

Abstract

The invention discloses a preparation method of a polyamide inhibitor for drilling fluid, which comprises the following steps: a. adding a substance A and deionized water into a container, and heating to completely dissolve the substance A; b. adding the substance B into another container, and heating to completely dissolve the substance B; c. slowly pouring the solution of the substance B into the substance A, stirring for 2-3 h, and evaporating the solvent to obtain an intermediate product; d. dissolving a proper amount of intermediate product in deionized water, adding a substance A and a catalyst, and introducing nitrogen to remove oxygen in a system; e. heating to 150-180 ℃, reacting at constant temperature for 1h, heating to 230 ℃, reacting for 2h, vacuumizing to 0.01atm, heating to 270 ℃, removing a heat source after reacting for 4h, keeping vacuum, and cooling to obtain a brown yellow viscous substance, namely a product; the inhibitor prepared by the preparation method has good compatibility with the conventional water-based treating agent, has small influence on the performance of the water-based drilling fluid, and can effectively strengthen the inhibiting capability of the water-based drilling fluid.

Description

A kind of preparation method of polyamides amine inhibitors for drilling fluid
Technical field
The present invention relates to drilling fluid inhibitor technical field, specifically relates to a kind of polyamide for drilling fluid and presses down The preparation method of preparation.
Background technology
When the water-sensitive stratas such as mud stone, shale are crept into using water-base drilling fluid, the easy hydration swelling of subterranean minerals, disperse, The problems such as so as to cause borehole well instability, drilling fluid rheology unmanageable.So the inhibition of drilling fluid system turns into probing water The key on quick property stratum.Meanwhile as the shale gas well scope drilled at present constantly expands, quantity is on the increase, wellbore fluid The inhibition of system becomes a key factor of site safety drilling well.
Conventional water-base drilling fluid inhibitor is mainly sylvite, ammonium salt and amine(Ammonium)Birds of the same feather flock together compound inhibitors, although tool There is certain inhibition, but it is limited for mud stone scattered by force, inhibition.And in actual application, if can not be high Effect suppresses the scattered of mud stone, the surface of clay after disperseing can rapid adsorption inhibitor, under causing the effective content of inhibitor rapid Drop, so as to cause the rejection ability of drilling fluid to decline rapidly.
Publication No. CN102504065A, publication date disclose a kind of brill for the Chinese patent literature on June 20th, 2012 Well liquid polyamine inhibitor and preparation method thereof;Initiator and acid-binding agent are placed in reactor, under normal pressure and nitrogen protection, Sulfonyl agent is added dropwise into reactor, carries out sulphur esterification, the reaction time is 10~12 hours, and sulphur esterification temperature is 0~30 DEG C, reactant is filtered, filtrate is soluble in water, after static split-phase, a layer liquid is removed, vacuum distillation goes to remove water, and obtains end sulphur Base ester compound;End sulfo group carboxylate is added drop-wise in the reactor equipped with aminating agent and precipitating reagent and carries out aminating reaction, reaction 2~ 3 hours, amination temperature was 70~90 DEG C, and product is filtered, and is evaporated under reduced pressure desolvation, obtains polyamine inhibitor;The additive is fitted It for a variety of water-base drilling fluids, can be good at controlling the aquation of mud shale to disperse, effectively reduce because shale hydration disperses The problems such as drilling fluid brought thickens, property of drilling fluid deteriorates, to realize that safe and efficient drilling well provides certain guarantee.
But be the conventional inhibitor of representative due to limited sorption capacity using above-mentioned patent document, frequently result in high temperature Lower generation desorption, so as to cause to lose inhibitory action under high temperature.So to solve the problems, such as the suppression of drilling fluid, it is necessary to research and develop Specifically for the water-base drilling fluid high temperature resistance inhibitor of water-sensitive formation drilling well, effectively reduce borehole well instability and landwaste aquation disperseed, Meet the technology needs of live water-sensitive strata high-quality and safety rapid drilling, improve exploration and development benefit.
The content of the invention
It is contemplated that the defects of present in above-mentioned prior art and deficiency, there is provided a kind of polyamides for drilling fluid The preparation method of amine inhibitors, the inhibitor prepared using this preparation method is good with conventional water base inorganic agent compatibility, to water Base drilling fluid performance impact is small, and the rejection ability of energy efficient hardening water-base drilling fluid, reaches and suppresses water-sensitive formation fossil water Change scattered effect, so as to reduce drilling cost, ensure drilling safety and speed.
The present invention is realized by using following technical proposals:
The preparation method of a kind of polyamides amine inhibitors for drilling fluid, it is characterised in that step is as follows:
A, substance A and deionized water are added in a reservoir, and being slowly heated under the conditions of not higher than 55 DEG C is completely dissolved substance A;
B, substance B is added in another container, the ratio of the amount of the material of substance B and substance A is 1 ~ 1.2:1, and alcoholic solvent is added, Heated under the conditions of not higher than 50 DEG C, be completely dissolved substance B;
C, in the case where rapidly stirring, the solution of substance B is poured slowly into substance A while hot, 2 ~ 3h is stirred, steams solvent, in being Between product;
D, appropriate intermediate product is taken to be dissolved in deionized water, additive A, catalyst, the addition of catalyst is substance A 1Wt%, the oxygen being passed through in nitrogen removal system;
E, 150 ~ 180 DEG C, isothermal reaction 1h are heated to, then is warming up to 230 DEG C, 2h is reacted, vacuumizes 0.01atm, is heated up 270 DEG C, thermal source is removed in reaction 4h recession, keeps vacuum, cooling, brown color thick substances are product;
Substance A is ethylenediamine, Putriscine, one kind in hexamethylene diamine;
Substance B is ethanedioic acid, adipic acid, one kind in the binary acid such as decanedioic acid;
Catalyst is sodium hypophosphite;
Alcoholic solvent nail alcohol, ethanol or isopropanol.
Compared with prior art, what the present invention was reached has the beneficial effect that:
By the checking of embodiment, it can learn that it has the following technical effect that:
1st, polyamides amine inhibitors, mud shale landwaste rolling rate of recovery can be made(150℃)Up to 75.23%, there is good suppression to make With the rheological characteristic of drilling fluid system and the stabilization of leak-off wall building property can be kept;
2nd, polyamides amine inhibitors and conventional treatment agent compatibility are good, influence little, drilling well liquid stream to the overall performance of drilling fluid Denaturation, leak-off wave making machine are substantially unaffected;
3rd, polyamides amine inhibitors have good temperature resistance, and temperature resistance is up to 150 DEG C.
In summary, using this method prepare polyamides amine inhibitors have high temperature resistance, inhibition significantly, to rheological characteristic The features such as small is influenceed, suitable for various water base drilling fluid systems.It can not only prevent that water-sensitive formation clay mineral aquation is scattered, swollen It borehole well instability problem caused by swollen, can also effectively stablize the rheological characteristic of drilling fluid system, avoid generation performance out of control.In addition, For the inhibitor in drilling fluid system, for dosage with safeguarding that dosage is small, expense is low, can significantly save drilling fluid cost.With multiple The continuous expansion of drilling well scale under miscellaneous geological conditions, the polyamides amine inhibitors market application foreground is wide, has good economy Benefit.
Embodiment
Embodiment 1:
A certain amount of ethylenediamine and deionized water are added in a reservoir, are slowly heated(Not higher than 55 DEG C)It is allowed to be completely dissolved;
Ethanedioic acid is added in another container(With the ratio position of the amount of the material of ethylenediamine(1~1.2):1), add a certain amount of first Alcoholic solvent, heating(Not higher than 50 DEG C), it is allowed to be completely dissolved;
In the case where rapidly stirring, the solution of ethanedioic acid is poured slowly into ethylenediamine while hot, 2 ~ 3h is stirred, steams solvent, in being Between product.
Take a certain amount of intermediate product to be dissolved in deionized water, add a small amount of ethylenediamine, Sodium Hypophosphite catalyst(For ethylenediamine 1Wt%), it is passed through nitrogen bubble 3min, the oxygen in removal system;
150 ~ 180 DEG C, isothermal reaction 1h are heated to, then is warming up to 230 DEG C, reacts 2h, vacuumizes 0.01atm, heating 270 DEG C, thermal source is removed in reaction 4h recession, keeps vacuum, cooling, brown color thick substances are product.
Embodiment 2:
A certain amount of Putriscine and deionized water are added in a reservoir, are slowly heated(Not higher than 55 DEG C)It is allowed to completely molten Solution;
Adipic acid is added in another container(With the ratio position of the amount of the material of Putriscine(1~1.2):1), add a certain amount of Methanol solvate, heating(Not higher than 50 DEG C), it is allowed to be completely dissolved;
In the case where rapidly stirring, the solution of adipic acid is poured slowly into Putriscine while hot, 2 ~ 3h is stirred, steams solvent, i.e., For intermediate product.
Take a certain amount of intermediate product to be dissolved in deionized water, add a small amount of Putriscine, Sodium Hypophosphite catalyst(For 1, The 1Wt% of 4- butanediamine), it is passed through nitrogen bubble 3min, the oxygen in removal system;
150 ~ 180 DEG C, isothermal reaction 1h are heated to, then is warming up to 230 DEG C, reacts 2h, vacuumizes 0.01atm, heating 270 DEG C, thermal source is removed in reaction 4h recession, keeps vacuum, cooling, brown color thick substances are product.
Embodiment 3:
A certain amount of hexamethylene diamine and deionized water are added in a reservoir, are slowly heated(Not higher than 55 DEG C)It is allowed to be completely dissolved;
Adipic acid is added in another container(With the ratio position of the amount of the material of hexamethylene diamine(1~1.2):1), add a certain amount of first Alcoholic solvent, heating(Not higher than 50 DEG C), it is allowed to be completely dissolved;
In the case where rapidly stirring, the solution of adipic acid is poured slowly into hexamethylene diamine while hot, 2 ~ 3h is stirred, steams solvent, in being Between product.
Take a certain amount of intermediate product to be dissolved in deionized water, add a small amount of hexamethylene diamine, Sodium Hypophosphite catalyst(For Isosorbide-5-Nitrae-fourth The 1Wt% of diamines), it is passed through nitrogen bubble 3min, the oxygen in removal system;
150 ~ 180 DEG C, isothermal reaction 1h are heated to, then is warming up to 230 DEG C, reacts 2h, vacuumizes 0.01atm, heating 270 DEG C, thermal source is removed in reaction 4h recession, keeps vacuum, cooling, brown color thick substances are product.
Embodiment method of evaluating performance
1st, polyamides amine inhibitors rolling rate of recovery is tested
4 parts of 350mL distilled water are taken, wherein three parts of polyamides amine inhibitors for being separately added into 1%(Embodiment 1), 7% conventional inhibitor Potassium chloride and 40% conventional inhibitor potassium formate, in low-speed agitator(1000rpm/min)Upper stirring 10min.By four parts of liquid Body is poured into ageing can, then is separately added into 50g mud shale landwaste.The rolling rate of recovery of four parts of liquid is determined at 150 DEG C, as a result Such as table 2:
The polyamides amine inhibitors of table 1 contrast with other conventional inhibitor mud shale landwaste rolling rate of recoveries
From table 1, the landwaste rolling rate of recovery of clear water is only 15.64%, and the rolling rate of recovery of the potassium chloride of conventional inhibitor 7% For 27.52%, 40% potassium formate is 58.42%.And 1% polyamides amine inhibitors are only added, landwaste rolling rate of recovery is 75.23%.It is real Test result to show, polyamides amine inhibitors have the excellent ability for suppressing hydration of mud stone and disperseing under 150 DEG C of environment.
2nd, influence of the polyamides amine inhibitors to drilling fluid system combination property
Influence of the polyamides amine inhibitors of table 2 to drilling fluid system combination property
System forms Basic sulfonation system Sulfonation system -1 Sulfonation system -2 Sulfonation system -3
Bentonite, % 2 2 2 2
Embodiment 2#, % 1 0.5 0
Embodiment 3#, % 0 0.5 1
SMP-2,% 4 4 4 4
SPNH,% 2 2 2 2
RSTF,% 2 2 2 2
Anti-seize lubricant, % 1 1 1 1
Performance 150 DEG C of aging 16h 150 DEG C of aging 16h 150 DEG C of aging 16h 150 DEG C of aging 16h
Density, g/ml 2.1 2.1 2.1 2.1
AV/ mPa.s 59 64 65 68
PV/ mPa.s 47 55 54 57
YP/Pa 12 9 11 11
Gel/(10’/10”) 1.5/5 2/6 3/8 4/9
FL/HPHT 8.2 8.0 8.5 8.3
Rolling rate of recovery, % 74.32 80.54 84.70 84.52
As can be seen from Table 2, after adding polyamides amine inhibitors in Common sulfonation system, rolling rate of recovery is significantly raised, indicates Polyamides amine inhibitors have good inhibition, and the inhibition of drilling fluid can be substantially improved.With the stream of basic sulfonation system Denaturation is compared with leak-off wave making machine, and after adding polyamides amine inhibitors, the leak-off wave making machine of drilling fluid system does not have significant change, and Rheological characteristic slightly rises, but unobvious, illustrates that polyamides amine inhibitors influence on the rheological characteristic of drilling fluid system with leak-off wave making machine Less, the inhibitor has good compatibility.

Claims (5)

1. the preparation method of a kind of polyamides amine inhibitors for drilling fluid, it is characterised in that step is as follows:
A, substance A and deionized water are added in a reservoir, and being heated under the conditions of not higher than 55 DEG C is completely dissolved substance A;
B, substance B is added in another container, the ratio of the amount of the material of substance B and substance A is 1 ~ 1.2:1, and alcoholic solvent is added, Heated under the conditions of not higher than 50 DEG C, be completely dissolved substance B;
C, the solution of substance B is poured into substance A, stirs 2 ~ 3h, steam solvent, as intermediate product;
D, appropriate intermediate product is taken to be dissolved in deionized water, additive A, catalyst, the addition of catalyst is substance A 1Wt%, the oxygen being passed through in nitrogen removal system;
E, 150 ~ 180 DEG C, isothermal reaction 1h are heated to, then is warming up to 230 DEG C, 2h is reacted, vacuumizes 0.01atm, is heated up 270 DEG C, thermal source is removed in reaction 4h recession, keeps vacuum, cooling, brown color thick substances are product.
A kind of 2. preparation method of polyamides amine inhibitors for drilling fluid according to claim 1, it is characterised in that:Thing Matter A is ethylenediamine, Putriscine, one kind in hexamethylene diamine.
A kind of 3. preparation method of polyamides amine inhibitors for drilling fluid according to claim 1, it is characterised in that:Thing Matter B is ethanedioic acid, adipic acid, one kind in the binary acid such as decanedioic acid.
A kind of 4. preparation method of polyamides amine inhibitors for drilling fluid according to claim 1, it is characterised in that:Urge Agent is sodium hypophosphite.
A kind of 5. preparation method of polyamides amine inhibitors for drilling fluid according to claim 1, it is characterised in that:Alcohol Solvent nail alcohol, ethanol or isopropanol.
CN201711076418.0A 2017-11-06 2017-11-06 Preparation method of polyamide inhibitor for drilling fluid Pending CN107652951A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111320972A (en) * 2018-12-13 2020-06-23 中石化石油工程技术服务有限公司 Amido chitosan, preparation method thereof and drilling fluid

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4757131A (en) * 1986-07-22 1988-07-12 Stamicarbon B.V. Production of high-molecular polytetramethylene adipamide pellet
US5371174A (en) * 1991-09-24 1994-12-06 Dsm N.V. Process for the production of polytetramethylene adipamides
CN102167815A (en) * 2011-01-21 2011-08-31 暨南大学 Method for preparing high-molecular-weight nylon-46 in supercritical carbon dioxide
CN104114670A (en) * 2012-02-14 2014-10-22 罗地亚运作公司 Novel agent for inhibiting the swelling of clays, compositions comprising said agent and methods implementing said agent
CN104592958A (en) * 2014-10-31 2015-05-06 中国石油化工集团公司 Powdery emulsifier for oil-based drilling fluid
CN104937068A (en) * 2013-02-07 2015-09-23 陶氏环球技术有限责任公司 Polyaminopolyamide-epichlorohydrin resins for use as clay and shale inhibition agents for the drilling industry

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4757131A (en) * 1986-07-22 1988-07-12 Stamicarbon B.V. Production of high-molecular polytetramethylene adipamide pellet
US5371174A (en) * 1991-09-24 1994-12-06 Dsm N.V. Process for the production of polytetramethylene adipamides
CN102167815A (en) * 2011-01-21 2011-08-31 暨南大学 Method for preparing high-molecular-weight nylon-46 in supercritical carbon dioxide
CN104114670A (en) * 2012-02-14 2014-10-22 罗地亚运作公司 Novel agent for inhibiting the swelling of clays, compositions comprising said agent and methods implementing said agent
CN104937068A (en) * 2013-02-07 2015-09-23 陶氏环球技术有限责任公司 Polyaminopolyamide-epichlorohydrin resins for use as clay and shale inhibition agents for the drilling industry
CN104592958A (en) * 2014-10-31 2015-05-06 中国石油化工集团公司 Powdery emulsifier for oil-based drilling fluid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111320972A (en) * 2018-12-13 2020-06-23 中石化石油工程技术服务有限公司 Amido chitosan, preparation method thereof and drilling fluid
CN111320972B (en) * 2018-12-13 2022-11-18 中石化石油工程技术服务有限公司 Amido chitosan, preparation method thereof and drilling fluid

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Application publication date: 20180202