CN109749723B - High-temperature-resistant emulsifier for oil-based drilling fluid, preparation method and application - Google Patents
High-temperature-resistant emulsifier for oil-based drilling fluid, preparation method and application Download PDFInfo
- Publication number
- CN109749723B CN109749723B CN201711082088.6A CN201711082088A CN109749723B CN 109749723 B CN109749723 B CN 109749723B CN 201711082088 A CN201711082088 A CN 201711082088A CN 109749723 B CN109749723 B CN 109749723B
- Authority
- CN
- China
- Prior art keywords
- oil
- emulsifier
- sulfonate
- based drilling
- drilling fluid
- 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
Links
- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 66
- 238000005553 drilling Methods 0.000 title claims abstract description 41
- 239000012530 fluid Substances 0.000 title claims abstract description 36
- 238000002360 preparation method Methods 0.000 title abstract description 9
- BTXXTMOWISPQSJ-UHFFFAOYSA-N 4,4,4-trifluorobutan-2-one Chemical compound CC(=O)CC(F)(F)F BTXXTMOWISPQSJ-UHFFFAOYSA-N 0.000 claims abstract description 23
- BQACOLQNOUYJCE-FYZZASKESA-N Abietic acid Natural products CC(C)C1=CC2=CC[C@]3(C)[C@](C)(CCC[C@@]3(C)C(=O)O)[C@H]2CC1 BQACOLQNOUYJCE-FYZZASKESA-N 0.000 claims abstract description 22
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims abstract description 22
- 238000003756 stirring Methods 0.000 claims abstract description 15
- 150000008052 alkyl sulfonates Chemical class 0.000 claims abstract description 13
- 239000003513 alkali Substances 0.000 claims abstract description 10
- 238000006243 chemical reaction Methods 0.000 claims abstract description 9
- 238000001816 cooling Methods 0.000 claims abstract description 9
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 238000002156 mixing Methods 0.000 claims abstract description 9
- 238000004090 dissolution Methods 0.000 claims abstract description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 17
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 15
- 239000011575 calcium Substances 0.000 claims description 12
- 229910052791 calcium Inorganic materials 0.000 claims description 12
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 9
- -1 alkyl carbon Chemical compound 0.000 claims description 9
- 239000000292 calcium oxide Substances 0.000 claims description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 9
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 8
- 239000003208 petroleum Substances 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 7
- 229940077388 benzenesulfonate Drugs 0.000 claims description 5
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 5
- 239000000920 calcium hydroxide Substances 0.000 claims description 5
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 5
- 150000004996 alkyl benzenes Chemical class 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 239000011591 potassium Substances 0.000 claims description 2
- 229910052700 potassium Inorganic materials 0.000 claims description 2
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 claims description 2
- 229910001950 potassium oxide Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 2
- 229910001948 sodium oxide Inorganic materials 0.000 claims description 2
- 239000006227 byproduct Substances 0.000 abstract description 6
- 230000001804 emulsifying effect Effects 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 54
- 235000014113 dietary fatty acids Nutrition 0.000 description 7
- 239000000194 fatty acid Substances 0.000 description 7
- 229930195729 fatty acid Natural products 0.000 description 7
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 description 5
- 239000002199 base oil Substances 0.000 description 5
- 229940083575 sodium dodecyl sulfate Drugs 0.000 description 5
- 235000019333 sodium laurylsulphate Nutrition 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 3
- RSWGJHLUYNHPMX-ONCXSQPRSA-N abietic acid Chemical compound C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C(O)=O RSWGJHLUYNHPMX-ONCXSQPRSA-N 0.000 description 3
- 150000001336 alkenes Chemical class 0.000 description 3
- 239000002283 diesel fuel Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 239000012752 auxiliary agent Substances 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 229920000768 polyamine Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002193 fatty amides Chemical class 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
Abstract
The invention discloses a high-temperature resistant emulsifier for oil-based drilling fluid, a preparation method and application. The emulsifier comprises abietic acid, white oil, alkali and alkyl sulfonate; the components are calculated according to the parts by weight: 100 parts of white oil; 40-100 parts of abietic acid; 4-17 parts by weight of an alkali; 5-60 parts of alkyl sulfonate. The preparation method comprises the following steps: mixing and heating abietic acid and white oil to 30-100 ℃, stirring for full dissolution, adding alkali for reaction at 30-100 ℃ for 1-4 hours, then adding alkyl sulfonate for reaction for 1-4 hours, and cooling to obtain the high-temperature resistant emulsifier. The emulsifier disclosed by the invention can resist the temperature of more than 200 ℃, and has a good emulsifying effect; and the reaction condition is mild, the renewable resources can be recycled, the added value of the by-products is greatly improved, and the method has great economic and social significance.
Description
Technical Field
The invention relates to the technical field of oil-based drilling fluids, and further relates to a high-temperature-resistant emulsifier for an oil-based drilling fluid, a preparation method and application.
Background
The oil-based drilling fluid has the advantages of strong inhibition, excellent lubricity, contribution to well wall stability and the like, so that the oil-based drilling fluid becomes an important means for drilling high-difficulty high-temperature deep wells, large-inclination directional wells, horizontal wells and various wells with complex structures, and has an important position in the global drilling fluid market.
In the oil-based drilling fluid, a dispersed phase (water phase) is uniformly dispersed in a continuous phase (oil phase) mainly by virtue of an emulsifier, so that the stability of an oil-based drilling fluid system is directly determined by the quality of the performance of the emulsifier, and the rheological property and the filtration loss of the oil-based drilling fluid are also greatly influenced.
At present, the emulsifier for the domestic oil-based drilling fluid is mainly sorbitan fatty acid esters and polyamides. For example, chinese patent publication No. 104449598A discloses "a viscosifying emulsifier for oil-based drilling fluids and a method for preparing the same", which comprises sorbitan fatty acid esters, fatty acid glycerides, polyethylene derivatives, and the like as main components. Chinese patent 102027092a discloses "polyamide emulsifiers based on polyamines and fatty acids/carboxylic acids for oil-based drilling fluids" whose main component is the reaction product of fatty acids with polyamines and mono (poly) polycarboxylic acids. The sorbitan fatty acid ester emulsifier mainly has the defects of easy decomposition and failure under a high-temperature condition, and particularly needs to be continuously maintained and replenished when the sorbitan fatty acid ester emulsifier is used in deep well drilling engineering at the temperature of more than 150 ℃ in an alkaline system environment of oil-based drilling fluid; for the polyamide emulsifier, the emulsifier has a good emulsifying effect at high temperature, but adopts various raw materials, and has a complex preparation process and high production cost.
Disclosure of Invention
In order to solve the problems in the prior art, the invention provides a high-temperature resistant emulsifier for an oil-based drilling fluid, a preparation method and application. The forestry byproduct rosin acid is used as a main raw material, and the high-temperature-resistant emulsifier for the oil-based drilling fluid is prepared through a reasonable route and mild reaction conditions, so that the reutilization of renewable resources is facilitated, and the added value of the byproduct is greatly improved. Has great economic and social significance.
The invention aims to provide a high-temperature resistant emulsifier for an oil-based drilling fluid.
The emulsifier comprises:
abietic acid, white oil, alkali and alkyl sulfonate;
the components are calculated according to the parts by weight:
the alkali can react with abietic acid to produce abietic acid salt with emulsifying effect, preferably one or combination of calcium oxide, sodium oxide, potassium oxide, calcium hydroxide, sodium hydroxide and potassium hydroxide.
The white oil has the effect of a disperse phase, so that the high-temperature emulsifier has good fluidity and is convenient for construction on a drilling operation site, particularly in a low-temperature and high-cold environment. The white oil can be industrial grade 3#, 5#, 7#, 10#, 15# white oil and their mixture;
the alkyl sulfonate can play a role in assisting emulsification, and is one or a combination of alkyl benzene sulfonate, alkyl sulfonate or petroleum sulfonate; the carbon number of the alkyl group of the alkyl sulfonate is preferably 6-40; the sulfonate is preferably one or a mixture of calcium sulfonate, sodium sulfonate and potassium sulfonate.
The invention also aims to provide a preparation method of the high-temperature resistant emulsifier for the oil-based drilling fluid. The method comprises the following steps:
mixing and heating abietic acid and white oil to 30-100 ℃, stirring for full dissolution, adding alkali for reaction at 30-100 ℃ for 1-4 hours, then adding alkyl sulfonate for reaction for 1-4 hours, and cooling to obtain the high-temperature resistant emulsifier.
The invention also aims to provide the application of the high-temperature resistant emulsifier for the oil-based drilling fluid in petroleum drilling.
The high-temperature resistant emulsifier can be used as an emulsifier of an oil-based drilling fluid system using diesel oil, white oil, alpha-long-chain olefin, refined mineral oil, gas oil and a mixture thereof as base oil, the addition amount is 2-6%, and the temperature resistance can reach 220 ℃.
ADVANTAGEOUS EFFECTS OF INVENTION
1. The emulsifier for the high-temperature-resistant oil-based drilling fluid is prepared by utilizing the forestry byproduct rosin acid through a simple reaction process, so that the production process is greatly simplified and the cost is reduced compared with the conventional multipurpose fatty amide emulsifier.
2. The emulsifier can be applied to an oil-based drilling fluid system taking diesel oil, white oil, alpha-long chain olefin, long chain ester, gas oil and a mixture thereof as base oil, has good emulsifying effect and can resist the temperature of 220 ℃.
3. The main raw material rosin acid of the emulsifier is a byproduct of forestry resources, which is beneficial to the reutilization of renewable resources and realizes the great increase of the added value of the byproduct.
Detailed Description
The present invention will be further described with reference to the following examples.
The present invention is by no means limited to the following examples.
Example 1: preparation of the emulsifiers according to the invention
(1) The emulsifier of the invention is a composition of alkali, abietic acid, white oil and alkyl sulfonate.
(2) The main materials used in this example are as follows: abietic acid is produced by Zhengzhou Jiahong chemical products limited company, white oil is a product of Chinese petrochemical Yanshan petrochemical company, sodium dodecyl sulfate is chemically pure by Beijing chemical reagent company, calcium alkylbenzene sulfonate is produced by a Chen Taiwan auxiliary agent factory, calcium petroleum sulfonate is produced by the Chen Taiwan auxiliary agent factory, and calcium oxide, calcium hydroxide, sodium hydroxide and potassium hydroxide are all chemically pure by the Beijing chemical reagent company.
(3) The composition of the emulsifier of this example is as follows:
emulsifier 1: calcium oxide, abietic acid, white oil and sodium dodecyl sulfate in a ratio of 17:100:100: 5;
emulsifier 2: calcium hydroxide, abietic acid, white oil and sodium dodecyl sulfate in a ratio of 4:40:100: 60;
emulsifier 3: sodium hydroxide, abietic acid, white oil and calcium petroleum sulfonate in the weight ratio of 7:40:100: 45;
emulsifier 4: potassium hydroxide, abietic acid, white oil and calcium petroleum sulfonate in the weight ratio of 10 to 50 to 100 to 20;
emulsifier 5: calcium oxide, abietic acid, white oil and calcium alkyl benzene sulfonate in the weight ratio of 5 to 40 to 100 to 60;
emulsifier 6: the weight ratio of sodium hydroxide, abietic acid, white oil and calcium alkyl benzene sulfonate is 12:50:100: 25.
(4) The emulsifier of this example was prepared as follows:
emulsifier 1: mixing abietic acid and white oil, heating to 30 deg.C, stirring for dissolving, adding calcium oxide, reacting at 100 deg.C for 4 hr, adding sodium dodecylsulfate, reacting for 1 hr, and cooling to obtain high temperature resistant emulsifier 1.
Emulsifier 2: mixing abietic acid and white oil, heating to 60 deg.C, stirring for dissolving, adding calcium hydroxide, reacting at 100 deg.C for 4 hr, adding sodium dodecylsulfate, reacting for 2 hr, and cooling to obtain high temperature resistant emulsifier 2.
Emulsifier 3: mixing abietic acid and white oil, heating to 80 deg.C, stirring for dissolving, adding sodium hydroxide, reacting at 80 deg.C for 2 hr, adding calcium petroleum sulfonate, reacting for 2 hr, and cooling to obtain high temperature resistant emulsifier 3.
Emulsifier 4: mixing abietic acid and white oil, heating to 100 deg.C, stirring for dissolving, adding potassium hydroxide, reacting at 100 deg.C for 1 hr, adding calcium petroleum sulfonate, reacting for 1 hr, and cooling to obtain high temperature resistant emulsifier 4.
Emulsifier 5: mixing abietic acid and white oil, heating to 90 deg.C, stirring for dissolving, adding calcium oxide, reacting at 50 deg.C for 4 hr, adding calcium alkylbenzene sulfonate, reacting for 4 hr, and cooling to obtain high temperature resistant emulsifier 5.
Emulsifier 6: mixing abietic acid and white oil, heating to 100 deg.C, stirring for dissolving, adding sodium hydroxide, reacting at 30 deg.C for 4 hr, adding calcium alkyl benzene sulfonate, reacting for 3 hr, and cooling to obtain high temperature resistant emulsifier 6.
Example 2: the emulsifier of the invention is prepared into the oil-based drilling fluid
In order to effectively evaluate the effect of the emulsifier, an oil-based drilling fluid system is prepared by adopting the following formula, wherein the formula comprises the following components: 100 parts of base oil (diesel oil, white oil, alpha-long chain olefin, refined mineral oil and gas oil) and 33 parts of CaCl with the mass concentration of 25 percent2The additive comprises an aqueous solution, 5 parts of the emulsifier, 3 parts of CaO, 4 parts of organic soil and 4 parts of a filtrate reducer.
The formula is prepared according to the following steps:
putting base oil for the oil-based drilling fluid into a stirring cup, adding an emulsifier under strong stirring, and stirring at a high speed for 10 min; then adding CaCl2Stirring with saline water at high speed for 40 min; and then sequentially adding organic soil, calcium oxide and a fluid loss additive into the mixed system, strongly stirring each material for 20min after adding, and strongly stirring all the materials for 30min after adding to obtain the oil-based drilling fluid system.
Example 3: oil-based drilling fluid performance determination
The demulsification voltage ES, the plastic viscosity PV and the dynamic shear force YP of the oil-based drilling fluid system with different emulsifier configurations are determined according to GB/T16782-1997, and the test results are shown in Table 1.
TABLE 1 oil-based drilling fluid System Performance for different emulsifiers
Table 1 shows that after the emulsifier prepared by the invention is used in oil-based drilling fluid consisting of different base oils and the temperature is between 180 and 220 ℃, the emulsion breaking voltage ES is higher than 500V and far higher than the required threshold of emulsion stability of 400V, and the emulsifier has good emulsification effect.
Claims (5)
1. The high-temperature resistant emulsifier for the oil-based drilling fluid is characterized by consisting of abietic acid, white oil, alkali and alkyl sulfonate;
the components are calculated according to the parts by weight:
the alkali is one or a combination of calcium oxide, sodium oxide, potassium oxide, calcium hydroxide, sodium hydroxide and potassium hydroxide;
the alkyl sulfonate is one or a combination of alkyl benzene sulfonate or petroleum sulfonate;
the alkyl carbon number of the alkyl sulfonate is 6-40.
3. the high temperature resistant emulsifier for oil-based drilling fluids according to claim 1, wherein:
the sulfonate is one or mixture of calcium sulfonate, sodium sulfonate and potassium sulfonate.
4. A method for producing a high temperature resistant emulsifier for oil-based drilling fluid according to any one of claims 1 to 3, comprising:
mixing and heating abietic acid and white oil to 30-100 ℃, stirring for full dissolution, adding alkali for reaction at 30-100 ℃ for 1-4 hours, then adding alkyl sulfonate for reaction for 1-4 hours, and cooling to obtain the high-temperature resistant emulsifier.
5. Use of the high temperature resistant emulsifier for oil-based drilling fluid according to any one of claims 1 to 3 in oil drilling.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711082088.6A CN109749723B (en) | 2017-11-01 | 2017-11-01 | High-temperature-resistant emulsifier for oil-based drilling fluid, preparation method and application |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711082088.6A CN109749723B (en) | 2017-11-01 | 2017-11-01 | High-temperature-resistant emulsifier for oil-based drilling fluid, preparation method and application |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109749723A CN109749723A (en) | 2019-05-14 |
CN109749723B true CN109749723B (en) | 2021-06-22 |
Family
ID=66400815
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711082088.6A Active CN109749723B (en) | 2017-11-01 | 2017-11-01 | High-temperature-resistant emulsifier for oil-based drilling fluid, preparation method and application |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109749723B (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113667329B (en) * | 2021-08-12 | 2022-08-09 | 黄鑫 | High-permeability sand-fixing primer |
CN115772389B (en) * | 2021-09-06 | 2023-10-17 | 中国石油化工股份有限公司 | Low-temperature emulsifier composition, low-temperature emulsifier and preparation method thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB592754A (en) * | 1943-12-27 | 1947-09-29 | Shell Dev | Well drilling fluid |
GB1058943A (en) * | 1963-08-29 | 1967-02-15 | Shell Int Research | Method for increasing well drilling rate |
CN105062437A (en) * | 2015-08-03 | 2015-11-18 | 湖北汉科新技术股份有限公司 | 240DEG C high temperature resistant oil-in-water emulsion drilling fluid |
CN105874153A (en) * | 2013-11-19 | 2016-08-17 | 佐治亚-太平洋化工品有限公司 | Modified hydrocarbon resins as fluid loss additives |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103305196A (en) * | 2012-03-09 | 2013-09-18 | 长江大学 | Biodiesel-based drilling fluid |
CN103756652B (en) * | 2014-01-20 | 2016-05-25 | 中国石油集团川庆钻探工程有限公司工程技术研究院 | A kind of emulsifying agent and preparation method thereof for oil base drilling fluid |
CN106350040A (en) * | 2015-07-15 | 2017-01-25 | 中国石油化工股份有限公司 | High-temperature-resistant water-in-oil biodiesel drilling fluid and preparation method |
-
2017
- 2017-11-01 CN CN201711082088.6A patent/CN109749723B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB592754A (en) * | 1943-12-27 | 1947-09-29 | Shell Dev | Well drilling fluid |
GB1058943A (en) * | 1963-08-29 | 1967-02-15 | Shell Int Research | Method for increasing well drilling rate |
CN105874153A (en) * | 2013-11-19 | 2016-08-17 | 佐治亚-太平洋化工品有限公司 | Modified hydrocarbon resins as fluid loss additives |
CN105062437A (en) * | 2015-08-03 | 2015-11-18 | 湖北汉科新技术股份有限公司 | 240DEG C high temperature resistant oil-in-water emulsion drilling fluid |
Non-Patent Citations (3)
Title |
---|
An Analytical Method for Emulsifier Concentration in an Oil-Base Drilling Fluid;R. Matherly,;《Journal or Petroleum Technology》;19810801;第33卷(第8期);第1389-1393页 * |
国内外油基钻井液用乳化剂研究进展;郭鹏;《内蒙古石油化工》;20170830;第43卷(第8期);第5-8页 * |
油包水乳化剂的研究及其在有机钻井液中的应用;许馨;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20150215(第2期);第B019-28页 * |
Also Published As
Publication number | Publication date |
---|---|
CN109749723A (en) | 2019-05-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2834319B2 (en) | Use of selected lower carboxylate oils in drilling fluids. | |
CN109722230B (en) | Emulsifier for oil-based drilling fluid, preparation method of emulsifier and drilling fluid | |
CN104164224B (en) | A kind of inverse emulsion drilling fluid and its preparation method and application | |
CN101519585B (en) | Shearing cross-linking sensitive plugging agent and preparation method thereof | |
IE900448L (en) | Monocarboxylic acid methylesters in invert drilling muds | |
IE63532B1 (en) | Esters of carboxylic acids of medium chain-length as a component of the oil phase in invert drillingmuds | |
MX2012000471A (en) | Emulsion stabilizing agents for drilling and completion fluids. | |
CN103509541A (en) | Micro-emulsion viscosity reducer for thick oil, and preparation method thereof | |
CN104140792B (en) | A kind of oil base drilling fluid emulsifying agent and its preparation method and application | |
CN109749723B (en) | High-temperature-resistant emulsifier for oil-based drilling fluid, preparation method and application | |
CN111961457B (en) | Oil displacement complexing agent for heavy oil reservoir and preparation method and application thereof | |
CN104694103A (en) | A Surfactant Compound System with Reservoir Adaptability | |
CN102391841A (en) | Biodiesel drilling fluid lubricant and preparation method thereof | |
CN103013465B (en) | Polyhydroxy-structure emulsifier and oil-base drilling fluid containing same | |
CN111378419A (en) | High-temperature-resistant emulsifier for oil-based drilling fluid and preparation method thereof | |
CN103992784A (en) | Thickened oil emulsification viscosity reduction-demulsification compound and preparation method thereof | |
CN106634888A (en) | High water phase oil-based drilling fluid applicable to long horizontal section of shale gas and preparation method of high water phase oil-based drilling fluid | |
CN103642467B (en) | low-fluorescence anti-blocking lubricant for drilling fluid and preparation method thereof | |
CN106147729A (en) | A kind of oil base drilling fluid and preparation method thereof | |
CN108690598A (en) | A kind of shale gas water blanket base fracturing fluid and preparation method thereof | |
CN102504772B (en) | Biodiesel drilling fluid and preparation method thereof | |
CN114605973A (en) | Oil-based drilling fluid with high density and high dynamic-plastic ratio | |
CN102604621B (en) | Novel high-efficiency composite viscosity reducer for super heavy oil | |
CN105713591A (en) | inversely emulsified drilling fluid and preparation method | |
US11339317B1 (en) | Method of drilling a wellbore |
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 | ||
GR01 | Patent grant | ||
GR01 | Patent grant |