CN107974242A - A kind of drilling fluid tackifier - Google Patents
A kind of drilling fluid tackifier Download PDFInfo
- Publication number
- CN107974242A CN107974242A CN201711129679.4A CN201711129679A CN107974242A CN 107974242 A CN107974242 A CN 107974242A CN 201711129679 A CN201711129679 A CN 201711129679A CN 107974242 A CN107974242 A CN 107974242A
- Authority
- CN
- China
- Prior art keywords
- parts
- drilling fluid
- stirred
- oil
- dispersant
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/02—Well-drilling compositions
- C09K8/03—Specific additives for general use in well-drilling compositions
- C09K8/035—Organic additives
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2208/00—Aspects relating to compositions of drilling or well treatment fluids
- C09K2208/34—Lubricant additives
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Adhesives Or Adhesive Processes (AREA)
Abstract
The invention discloses a kind of drilling fluid tackifier, belong to technical field of petroleum extraction.Count in parts by weight, base oil is weighed successively, coal oil mixture, No. 1 additive, No. 2 additives, emulsifying agent, water, polyacrylamide and dispersant, by base oil, coal oil mixture, No. 1 additive and No. 2 additives are sequentially added in mixer, in temperature be 80~90 DEG C, rotating speed is stirred 25~45min under conditions of being 220~260r/min, obtain oil phase blank, by emulsifying agent, water, polyacrylamide and dispersant are sequentially added in mixer, in temperature be 45~55 DEG C, under conditions of rotating speed is 250~300r/min, it is stirred 15~30min, obtain water phase blank, water phase blank is instilled in oil phase blank with the speed of 12~15mL/min, and it is stirred, to the end of instillation, up to drilling fluid tackifier.Drilling fluid tackifier prepared by the present invention has excellent Efficient Adhesive Promotion, and has excellent lubricity.
Description
Technical field
The invention discloses a kind of drilling fluid tackifier, belong to technical field of petroleum extraction.
Background technology
Drilling fluid, is the various circulation of fluid general names for meeting drilling well need of work in drilling process with its multiple functions.Ground
The harsh environment of lower drillng operation promotes the research and development to drilling fluid, it is desirable to can be completed in drilling process following more
Item key task:Suspension, pressure control, rock stratum stability, buoyancy, lubrication and cooling.
Drilling fluid is different from the physicochemical property of cement mortar, in well cementation due to annular space stream etc. reason can cause both blend and
Contact stain is produced, slurry section fluid mobility occurs because chemistry is incompatible and deteriorates suddenly.The harm of contact stain is:Slurry
Section flow resistance increase influences replacement efficiency, and Lou weak floor may be pressed and cause cementing " low to return " and " leakage by being pumped quick rise
Envelope ";Slurry high thixotropic may cause " plant flag bar " accident etc..The technical measures for solving contact stain at present have:1. carry out well
Lower different fluid compatibility test, adjusts Working solution prescription repeatedly, to improve slurry mobility;2. adjustment property of drilling fluid simultaneously makes
Use insulating liquid.But deep well cementing practice have shown that, slurry is difficult to avoid that, and some additive for drilling fluid when mixing proportion is minimum still
It is one of insoluble basic reason of contact stain to cause slurry mobility to deteriorate.In terms of contact stain research, Ma Yong etc.
Drilling fluid and the incompatible reason of cement mortar chemistry are analyzed;Yang Xiangyan proposes " two slurries " and interferes model;Liu's generation
Refined grade has carried out the anti-pollution experiment of cementing slurry and has screened the additive for drilling fluid for having blood coagulation enhancing effect to cement mortar;Joel etc.
The property of drilling fluid after by cement contaminants is studied with Fakhreldin etc.;But the studies above does not verify contact stain also
Mechanism.It is maximum that Cementing Practices find that the additive for drilling fluid such as biological tackifier, KPAM, JD-6 influences cement mortar mobility.But
Be used the drilling fluids of tackifier also there are tackifier Efficient Adhesive Promotion it is bad the problem of, therefore also need to study it.
The content of the invention
The present invention solves the technical problem of:It is bad for traditional drilling fluid tackifier Efficient Adhesive Promotion, there is provided one
Kind drilling fluid tackifier.
In order to solve the above-mentioned technical problem, the technical solution adopted in the present invention is:
A kind of drilling fluid tackifier, is made of the raw material of following parts by weight:
30~45 parts of base oil
12~18 parts of coal oil mixture
No. 1 10~12 parts of additive
No. 2 10~15 parts of additives
4~8 parts of emulsifying agent
35~45 parts of water
6~10 parts of polyacrylamide
3~5 parts of dispersant
The preparation method of the coal oil mixture is:
By medium temperature coal tar and high temperature coal-tar in mass ratio 2:1~3:1 mixing, and add medium temperature coal tar quality 0.1~0.2
Modified cellulose again, is stirred, obtains coal oil mixture;
The preparation method of No. 1 additive is:
By Petropols and terpene resin in mass ratio 2:1~4:1 mixing, and add the knot of 0.4~0.6 times of Petropols quality
Cold glue, is stirred, and obtains No. 1 additive;
The preparation method of No. 2 additives is:
By organic siliconresin and paraffin in mass ratio 1:2~1:3 mixing, and add the catalysis of 0.06~0.07 times of organosilicon quality
Agent, is stirred, Freezing smashing, and sieving, obtains No. 2 additives;
The preparation method of the drilling fluid tackifier is:
(1)Formed by raw material and weigh each component;
(2)Base oil, coal oil mixture, No. 1 additive and No. 2 additives are stirred, oil phase blank is obtained, will emulsify
Agent, water, polyacrylamide and dispersant are stirred, and obtain water phase blank, water phase blank and oil phase blank are stirred, must bore
Well liquid tackifier.
The base oil is white oil, any one in dimethicone or soybean oil.
The emulsifying agent is sorbester p17, sorbester p18, any one or the combination of several of them in polysorbas20 and polysorbate60.
The dispersant is dispersant NNO, any one in Dispersant MF or dispersant 5040.
The modified cellulose is any one in hydroxymethyl cellulose or hydroxypropyl cellulose.
The Petropols are any one in C5 Petropols or C9 Petropols.
The catalyst is diethylenetriamine, any one in triethylene tetramine or ethylenediamine.
The beneficial effects of the invention are as follows:
(1)The present invention adds coal oil mixture when preparing drilling fluid tackifier, on the one hand, the medium temperature in coal oil mixture
Coal tar component can make the high temperature coal-tar component of coal oil mixture dispersed after adding in drilling fluid tackifier system
In drilling fluid tackifier system, also, medium temperature coal tar has certain suction-operated, so that thickening of the product to drilling fluid
Effect improves, and on the other hand, the high temperature coal-tar component in coal oil mixture has preferable adsorption capacity, is adding drilling well
After in liquid tackifier system, the Efficient Adhesive Promotion of drilling fluid tackifier can be effectively improved in use, therefore increase in drilling fluid
Coal oil mixture is added in stick can effectively improve the Efficient Adhesive Promotion and lubricity of drilling fluid tackifier;
(2)The present invention adds No. 1 additive and No. 2 additives when preparing drilling fluid tackifier, first, in No. 1 additive
Petropols can improve the greasy property of drilling fluid in use, and Petropols can coordinate terpene resin and tie cold
Glue, further improves the viscosity of drilling fluid, therefore adding No. 1 additive in drilling fluid tackifier can imitate the thickening of product
Fruit and greasy property further improve, and secondly, paraffin and organic siliconresin are contained in No. 2 additives, are adding drilling fluid thickening
After in agent system, after use, when drilling fluid temperature raises, No. 2 additives is paraffin melting in drilling fluid tackifier, promotes
The greasy property of product improves, and paraffin melting rear organic siliconresin appears, under the action of high temperature and curing agent, organosilicon
Resin can be partially cured, and cured resin can coat the impurity in system, while also the crack of the borehole wall can be filled out
Fill, and uncured resin can further improve the viscosity of drilling fluid due to higher crosslinking degree, therefore No. 2 additives
Addition can further improve the Efficient Adhesive Promotion of product and lubricity.
Embodiment
By medium temperature coal tar and high temperature coal-tar in mass ratio 2:1~3:1 is mixed in beaker, and into beaker in addition
The modified cellulose of warm 0.1~0.2 times of coal tar oil quality, beaker immigration digital display is tested the speed constant temperature blender with magnetic force, is in temperature
65~85 DEG C, under conditions of rotating speed is 220~280r/min, 35~50min is stirred, obtains coal oil mixture;By oil
Resin and terpene resin in mass ratio 2:1~4:1 is mixed in flask, and Petropols quality 0.4~0.6 is added into flask
Gellan gum again, is 85~95 DEG C in temperature, after rotating speed is stirred 40~60min under conditions of being 240~280r/min, obtains
No. 1 additive;By organic siliconresin and paraffin in mass ratio 1:2~1:3 mixing, and to organic siliconresin and the mixture of paraffin
The middle catalyst for adding 0.06~0.07 times of organosilicon quality, is 70~80 DEG C in temperature, rotating speed is the bar of 250~270r/min
After being stirred 45~55min under part, Freezing smashing, crosses 100~140 mesh sieves, obtains No. 2 additives;Count in parts by weight, successively
Weigh 30~45 parts of base oils, 12~18 parts of coal oil mixtures, 10~12 parts of No. 1 additives, 10~15 parts of No. 2 additives, 4
~8 parts of emulsifying agents, 35~45 parts of water, 6~10 parts of polyacrylamides and 3~5 parts of dispersants, by base oil, coal oil mixture,
No. 1 additive and No. 2 additives are sequentially added in mixer, are 80~90 DEG C in temperature, rotating speed is the bar of 220~260r/min
25~45min is stirred under part, obtains oil phase blank, emulsifying agent, water, polyacrylamide and dispersant are sequentially added into mixer
In, it is 45~55 DEG C in temperature, under conditions of rotating speed is 250~300r/min, is stirred 15~30min, obtains water phase blank,
Water phase blank is instilled in oil phase blank with the speed of 12~15mL/min, and is 70~85 DEG C in temperature, rotating speed for 220~
Under conditions of 300r/min, it is stirred, to the end of instillation, up to drilling fluid tackifier.The base oil is white oil, dimethyl
Any one in silicone oil or soybean oil.The emulsifying agent is sorbester p17, sorbester p18, any one in polysorbas20 and polysorbate60 or several
The combination of kind.The dispersant is dispersant NNO, any one in Dispersant MF or dispersant 5040.The modified cellulose
For any one in hydroxymethyl cellulose or hydroxypropyl cellulose.The Petropols is in C5 Petropols or C9 Petropols
Any one.The catalyst is diethylenetriamine, any one in triethylene tetramine or ethylenediamine.
Example 1
By medium temperature coal tar and high temperature coal-tar in mass ratio 3:1 is mixed in beaker, and medium temperature coal tar is added into beaker
The modified cellulose that 0.2 times of quality, beaker immigration digital display is tested the speed constant temperature blender with magnetic force, is 85 DEG C in temperature, rotating speed is
Under conditions of 280r/min, 50min is stirred, obtains coal oil mixture;By Petropols and terpene resin in mass ratio 4:1
Be mixed in flask, and the gellan gum of 0.6 times of Petropols quality added into flask, in temperature be 95 DEG C, rotating speed 280r/
After being stirred 60min under conditions of min, No. 1 additive is obtained;By organic siliconresin and paraffin in mass ratio 1:3 mixing, and to
The catalyst of 0.07 times of organosilicon quality is added in the mixture of organic siliconresin and paraffin, is 80 DEG C in temperature, rotating speed is
After being stirred 55min under conditions of 270r/min, Freezing smashing, crosses 140 mesh sieves, obtains No. 2 additives;Count in parts by weight,
45 parts of base oils, 18 parts of coal oil mixtures, 12 parts of No. 1 additives, 15 parts of No. 2 additives, 8 parts of emulsifying agents, 45 are weighed successively
Part water, 10 parts of polyacrylamides and 5 parts of dispersants, by base oil, coal oil mixture, No. 1 additive and No. 2 additives successively
Add in mixer, be 90 DEG C in temperature, rotating speed is stirred 45min under conditions of being 260r/min, oil phase blank is obtained, by breast
Agent, water, polyacrylamide and dispersant are sequentially added in mixer, are 55 DEG C in temperature, rotating speed is the condition of 300r/min
Under, 30min is stirred, obtains water phase blank, is instilled water phase blank in oil phase blank with the speed of 15mL/min, and in temperature
For 85 DEG C, under conditions of rotating speed is 300r/min, it is stirred, to the end of instillation, up to drilling fluid tackifier.The base oil
For white oil.The emulsifying agent is sorbester p17.The dispersant is dispersant NNO.The modified cellulose is hydroxymethyl cellulose.
The Petropols are C5 Petropols.The catalyst is diethylenetriamine.
Example 2
Medium temperature coal tar is added in beaker, and the modified cellulose of 0.2 times of medium temperature coal tar quality is added into beaker, will be burnt
Cup moves into digital display and tests the speed constant temperature blender with magnetic force, is 85 DEG C in temperature, under conditions of rotating speed is 280r/min, is stirred
50min, obtains coal oil mixture;By Petropols and terpene resin in mass ratio 4:1 is mixed in flask, and adds into flask
Enter the gellan gum of 0.6 times of Petropols quality, be 95 DEG C in temperature, rotating speed is stirred 60min under conditions of being 280r/min
Afterwards, No. 1 additive is obtained;By organic siliconresin and paraffin in mass ratio 1:3 mixing, and to organic siliconresin and the mixture of paraffin
The middle catalyst for adding 0.07 times of organosilicon quality, is 80 DEG C in temperature, rotating speed is stirred under conditions of being 270r/min
After 55min, Freezing smashing, crosses 140 mesh sieves, obtains No. 2 additives;Count in parts by weight, weigh 45 parts of base oils, 18 parts of coals successively
Blended tars, 12 parts of No. 1 additives, 15 parts of No. 2 additives, 8 parts of emulsifying agents, 45 parts of water, 10 parts of polyacrylamides and 5 parts points
Powder, base oil, coal oil mixture, No. 1 additive and No. 2 additives are sequentially added in mixer, in temperature be 90 DEG C,
Rotating speed is stirred 45min under conditions of being 260r/min, oil phase blank is obtained, by emulsifying agent, water, polyacrylamide and dispersant
Sequentially add in mixer, be 55 DEG C in temperature, under conditions of rotating speed is 300r/min, is stirred 30min, obtains water phase base
Material, is instilled water phase blank in oil phase blank with the speed of 15mL/min, and is 85 DEG C in temperature, and rotating speed is the bar of 300r/min
Under part, it is stirred, to the end of instillation, up to drilling fluid tackifier.The base oil is white oil.The emulsifying agent is sapn
80.The dispersant is dispersant NNO.The modified cellulose is hydroxymethyl cellulose.The Petropols are C5 oil trees
Fat.The catalyst is diethylenetriamine.
Example 3
High temperature coal-tar is added in beaker, and the modified cellulose of 0.6 times of high temperature coal-tar quality is added into beaker, will be burnt
Cup moves into digital display and tests the speed constant temperature blender with magnetic force, is 85 DEG C in temperature, under conditions of rotating speed is 280r/min, is stirred
50min, obtains coal oil mixture;By Petropols and terpene resin in mass ratio 4:1 is mixed in flask, and adds into flask
Enter the gellan gum of 0.6 times of Petropols quality, be 95 DEG C in temperature, rotating speed is stirred 60min under conditions of being 280r/min
Afterwards, No. 1 additive is obtained;By organic siliconresin and paraffin in mass ratio 1:3 mixing, and to organic siliconresin and the mixture of paraffin
The middle catalyst for adding 0.07 times of organosilicon quality, is 80 DEG C in temperature, rotating speed is stirred under conditions of being 270r/min
After 55min, Freezing smashing, crosses 140 mesh sieves, obtains No. 2 additives;Count in parts by weight, weigh 45 parts of base oils, 18 parts of coals successively
Blended tars, 12 parts of No. 1 additives, 15 parts of No. 2 additives, 8 parts of emulsifying agents, 45 parts of water, 10 parts of polyacrylamides and 5 parts points
Powder, base oil, coal oil mixture, No. 1 additive and No. 2 additives are sequentially added in mixer, in temperature be 90 DEG C,
Rotating speed is stirred 45min under conditions of being 260r/min, oil phase blank is obtained, by emulsifying agent, water, polyacrylamide and dispersant
Sequentially add in mixer, be 55 DEG C in temperature, under conditions of rotating speed is 300r/min, is stirred 30min, obtains water phase base
Material, is instilled water phase blank in oil phase blank with the speed of 15mL/min, and is 85 DEG C in temperature, and rotating speed is the bar of 300r/min
Under part, it is stirred, to the end of instillation, up to drilling fluid tackifier.The base oil is white oil.The emulsifying agent is sapn
80.The dispersant is dispersant NNO.The modified cellulose is hydroxymethyl cellulose.The Petropols are C5 oil trees
Fat.The catalyst is diethylenetriamine.
Example 4
By medium temperature coal tar and high temperature coal-tar in mass ratio 3:1 is mixed in beaker, and medium temperature coal tar is added into beaker
The modified cellulose that 0.2 times of quality, beaker immigration digital display is tested the speed constant temperature blender with magnetic force, is 85 DEG C in temperature, rotating speed is
Under conditions of 280r/min, 50min is stirred, obtains coal oil mixture;By organic siliconresin and paraffin in mass ratio 1:3 is mixed
Close, and the catalyst of 0.07 times of organosilicon quality is added into the mixture of organic siliconresin and paraffin, be 80 DEG C in temperature, turn
After speed is stirred 55min under conditions of being 270r/min, Freezing smashing, crosses 140 mesh sieves, obtains No. 2 additives;In parts by weight
Meter, weigh successively 45 parts of base oils, 18 parts of coal oil mixtures, 15 parts of No. 2 additives, 8 parts of emulsifying agents, 45 parts of water, 10 parts it is poly-
Acrylamide and 5 parts of dispersants, base oil, coal oil mixture and No. 2 additives are sequentially added in mixer, are in temperature
90 DEG C, rotating speed be 260r/min under conditions of be stirred 45min, obtain oil phase blank, by emulsifying agent, water, polyacrylamide and
Dispersant is sequentially added in mixer, is 55 DEG C in temperature, under conditions of rotating speed is 300r/min, is stirred 30min, obtains water
Phase blank, is instilled water phase blank in oil phase blank with the speed of 15mL/min, and is 85 DEG C in temperature, rotating speed 300r/min
Under conditions of, it is stirred, to the end of instillation, up to drilling fluid tackifier.The base oil is white oil.The emulsifying agent is department
Disk 80.The dispersant is dispersant NNO.The modified cellulose is hydroxymethyl cellulose.The Petropols are C5 oil
Resin.The catalyst is diethylenetriamine.
Example 5
By medium temperature coal tar and high temperature coal-tar in mass ratio 3:1 is mixed in beaker, and medium temperature coal tar is added into beaker
The modified cellulose that 0.2 times of quality, beaker immigration digital display is tested the speed constant temperature blender with magnetic force, is 85 DEG C in temperature, rotating speed is
Under conditions of 280r/min, 50min is stirred, obtains coal oil mixture;By Petropols and terpene resin in mass ratio 4:1
Be mixed in flask, and the gellan gum of 0.6 times of Petropols quality added into flask, in temperature be 95 DEG C, rotating speed 280r/
After being stirred 60min under conditions of min, No. 1 additive is obtained;Count in parts by weight, weigh 45 parts of base oils, 18 parts of coals successively
Blended tars, 12 parts of No. 1 additives, 8 parts of emulsifying agents, 45 parts of water, 10 parts of polyacrylamides and 5 parts of dispersants, by base oil,
Coal oil mixture, No. 1 additive are sequentially added in mixer, are 90 DEG C in temperature, rotating speed stirs under conditions of being 260r/min
Mixing 45min is mixed, oil phase blank is obtained, emulsifying agent, water, polyacrylamide and dispersant is sequentially added in mixer, in temperature
For 55 DEG C, under conditions of rotating speed is 300r/min, 30min is stirred, obtains water phase blank, with the speed of 15mL/min by water phase
Blank is instilled in oil phase blank, and is 85 DEG C in temperature, under conditions of rotating speed is 300r/min, is stirred, to the end of instillation,
Up to drilling fluid tackifier.The base oil is white oil.The emulsifying agent is sorbester p17.The dispersant is dispersant NNO.Institute
It is hydroxymethyl cellulose to state modified cellulose.The Petropols are C5 Petropols.The catalyst is diethylenetriamine.
Comparative example:The drilling fluid tackifier of Suzhou Chemical Co., Ltd. production.
The gained of example 1 to 5 tackifier and comparative example product are subjected to performance detection, specific detection method is as follows:
Influence of the tackifier to drilling fluid fluidity is detected, measure is carried out according to GB/T5005, the specific testing result such as institute of table 1
Show:
Table 1
Detection content | Example 1 | Example 2 | Example 3 | Example 4 | Example 5 | Comparative example |
Use rear fluidity/cm | 12 | 16 | 18 | 15 | 16 | 24 |
From 1 testing result of table, drilling fluid tackifier prepared by the present invention has excellent Efficient Adhesive Promotion, and with excellent
Lubricity.
Claims (7)
- A kind of 1. drilling fluid tackifier, it is characterised in that:It is made of the raw material of following parts by weight:30~45 parts of base oil12~18 parts of coal oil mixtureNo. 1 10~12 parts of additiveNo. 2 10~15 parts of additives4~8 parts of emulsifying agent35~45 parts of water6~10 parts of polyacrylamide3~5 parts of dispersantThe preparation method of the coal oil mixture is:By medium temperature coal tar and high temperature coal-tar in mass ratio 2:1~3:1 mixing, and add medium temperature coal tar quality 0.1~0.2 Modified cellulose again, is stirred, obtains coal oil mixture;The preparation method of No. 1 additive is:By Petropols and terpene resin in mass ratio 2:1~4:1 mixing, and add the knot of 0.4~0.6 times of Petropols quality Cold glue, is stirred, and obtains No. 1 additive;The preparation method of No. 2 additives is:By organic siliconresin and paraffin in mass ratio 1:2~1:3 mixing, and add the catalysis of 0.06~0.07 times of organosilicon quality Agent, is stirred, Freezing smashing, and sieving, obtains No. 2 additives;The preparation method of the drilling fluid tackifier is:(1)Formed by raw material and weigh each component;(2)Base oil, coal oil mixture, No. 1 additive and No. 2 additives are stirred, oil phase blank is obtained, will emulsify Agent, water, polyacrylamide and dispersant are stirred, and obtain water phase blank, water phase blank and oil phase blank are stirred, must bore Well liquid tackifier.
- A kind of 2. drilling fluid tackifier according to claim 1, it is characterised in that:The base oil is white oil, dimethyl Any one in silicone oil or soybean oil.
- A kind of 3. drilling fluid tackifier according to claim 1, it is characterised in that:The emulsifying agent is sorbester p17, sapn 60, any one or the combination of several of them in polysorbas20 and polysorbate60.
- A kind of 4. drilling fluid tackifier according to claim 1, it is characterised in that:The dispersant is dispersant NNO, point Any one in powder MF or dispersant 5040.
- A kind of 5. drilling fluid tackifier according to claim 1, it is characterised in that:The modified cellulose is fine for methylol Any one in dimension element or hydroxypropyl cellulose.
- A kind of 6. drilling fluid tackifier according to claim 1, it is characterised in that:The Petropols are C5 Petropols Or any one in C9 Petropols.
- A kind of 7. drilling fluid tackifier according to claim 1, it is characterised in that:The catalyst is diethylenetriamine, Any one in triethylene tetramine or ethylenediamine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711129679.4A CN107974242A (en) | 2017-11-15 | 2017-11-15 | A kind of drilling fluid tackifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711129679.4A CN107974242A (en) | 2017-11-15 | 2017-11-15 | A kind of drilling fluid tackifier |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107974242A true CN107974242A (en) | 2018-05-01 |
Family
ID=62013474
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711129679.4A Pending CN107974242A (en) | 2017-11-15 | 2017-11-15 | A kind of drilling fluid tackifier |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107974242A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110734746A (en) * | 2019-12-20 | 2020-01-31 | 东营泰尔石油技术有限公司 | leak-proof leak-stopping adhesive |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1091751A (en) * | 1993-07-06 | 1994-09-07 | 大庆石油学院 | Water-soluble carbon pellet petroleum resin |
CN102083937A (en) * | 2008-07-03 | 2011-06-01 | 可泰克斯有限合伙公司 | Use, as thickening agent, of a salty aqueous formulation of a water-soluble cross-linked and hydrophobically-modified acrylic copolymer |
CN102898581A (en) * | 2012-09-20 | 2013-01-30 | 中国石油化工股份有限公司 | Temperature-resistant calcium-tolerant inverse emulsion polymer for drilling fluids and preparation method |
CN103113524A (en) * | 2013-02-16 | 2013-05-22 | 中国石油化工股份有限公司 | Preparation method of starch grafted copolymer inverse emulsion for drilling fluid |
CN104312573A (en) * | 2014-09-26 | 2015-01-28 | 孙安顺 | Crosslinking-free emulsion thickener for fracturing and preparation method thereof |
CN104710969A (en) * | 2015-04-03 | 2015-06-17 | 中国石油大学(北京) | Tackifier for oil-based drilling fluid and preparation method of tackifier |
CN105399884A (en) * | 2015-11-23 | 2016-03-16 | 中国石油天然气集团公司 | Downhole drilling emulsion lost circulation additive capable of becoming thicker when meeting water and preparation method of lost circulation additive |
CN106350041A (en) * | 2016-08-25 | 2017-01-25 | 中国石油集团渤海钻探工程有限公司 | Acrylamide polymer-oil base compounded system and application thereof as cement paste supporting liquid |
-
2017
- 2017-11-15 CN CN201711129679.4A patent/CN107974242A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1091751A (en) * | 1993-07-06 | 1994-09-07 | 大庆石油学院 | Water-soluble carbon pellet petroleum resin |
CN102083937A (en) * | 2008-07-03 | 2011-06-01 | 可泰克斯有限合伙公司 | Use, as thickening agent, of a salty aqueous formulation of a water-soluble cross-linked and hydrophobically-modified acrylic copolymer |
CN102898581A (en) * | 2012-09-20 | 2013-01-30 | 中国石油化工股份有限公司 | Temperature-resistant calcium-tolerant inverse emulsion polymer for drilling fluids and preparation method |
CN103113524A (en) * | 2013-02-16 | 2013-05-22 | 中国石油化工股份有限公司 | Preparation method of starch grafted copolymer inverse emulsion for drilling fluid |
CN104312573A (en) * | 2014-09-26 | 2015-01-28 | 孙安顺 | Crosslinking-free emulsion thickener for fracturing and preparation method thereof |
CN104710969A (en) * | 2015-04-03 | 2015-06-17 | 中国石油大学(北京) | Tackifier for oil-based drilling fluid and preparation method of tackifier |
CN105399884A (en) * | 2015-11-23 | 2016-03-16 | 中国石油天然气集团公司 | Downhole drilling emulsion lost circulation additive capable of becoming thicker when meeting water and preparation method of lost circulation additive |
CN106350041A (en) * | 2016-08-25 | 2017-01-25 | 中国石油集团渤海钻探工程有限公司 | Acrylamide polymer-oil base compounded system and application thereof as cement paste supporting liquid |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110734746A (en) * | 2019-12-20 | 2020-01-31 | 东营泰尔石油技术有限公司 | leak-proof leak-stopping adhesive |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103361042B (en) | Xanthan gum non-crosslinked fracturing liquid, Preparation Method And The Use | |
CN104232039B (en) | Multi-element synergistic plugging agent and application thereof | |
CN105482784A (en) | Oil-based drilling fluid plugging agent | |
CN104250546A (en) | Oil well dual crosslinking selective plugging agent | |
CN104087274A (en) | Multi-stage blocking pressure-bearing plugging agent | |
CN105419753A (en) | novel leakage-preventing while drilling agent for oil-based drilling fluid and application | |
CN1309798C (en) | Follow-drilling plugging agent and its preparation method and use | |
CN101381598B (en) | Fracture liquid and preparation method thereof | |
CN104449606A (en) | High temperature resistant well-cementing spacer fluid and preparation method thereof | |
CN101020817A (en) | Oil well cementing and blow-by preventing plugging fluid | |
CN102757778A (en) | Fracturing fluid capable of resisting high salinity water quality | |
CN107686723A (en) | CO (carbon monoxide)2Response in-situ gel channeling sealing sol and preparation method and application thereof | |
CN103756654B (en) | Salt-resistant high-density isolation liquid and preparation method thereof | |
CN106398669A (en) | Method for preparing pressure-bearing blocking agent for drilling fluid | |
CN106467736A (en) | A kind of fracturing fluid for shale pressure break and preparation method thereof | |
CN105802598B (en) | Modified alkali lignin plural gel blocking agent of a kind of polyacrylonitrile sodium salt and preparation method thereof | |
CN107974242A (en) | A kind of drilling fluid tackifier | |
CN107540260B (en) | Low-temperature cement early strength agent for well cementation and cement containing low-temperature cement early strength agent | |
CN106010495A (en) | Decompression and augmented injection agent for water injection wells and preparation method thereof | |
CN102181008B (en) | Water absorption resin for well repair and leaking stoppage and synthesis method thereof | |
CN109652036A (en) | A kind of high-temperature high-density high salinity water-base drilling fluid | |
CN107474817A (en) | A kind of Supramolecular self assembly fracturing fluid | |
CN110408372A (en) | Medium-low temperature oil-based solidified leakage-stopping slurry and preparation method thereof | |
CN105754565A (en) | Organic microsphere and inorganic silicate compounded type channeling sealing agent for thermal extraction of heavy oil and preparation method of channeling sealing agent | |
CN110373169A (en) | Time-controllable solidified oil-based leakage-stopping slurry and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180501 |
|
WD01 | Invention patent application deemed withdrawn after publication |