CN102241804A - Preparation method of coupling phenolic resin used for drilling fluid - Google Patents
Preparation method of coupling phenolic resin used for drilling fluid Download PDFInfo
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- CN102241804A CN102241804A CN 201110121858 CN201110121858A CN102241804A CN 102241804 A CN102241804 A CN 102241804A CN 201110121858 CN201110121858 CN 201110121858 CN 201110121858 A CN201110121858 A CN 201110121858A CN 102241804 A CN102241804 A CN 102241804A
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Abstract
The invention relates to a preparation method of coupling phenolic resin used for a drilling fluid, and the method comprises the following steps: successively adding 100 parts of phenol and 60 parts to 200 parts of formaldehyde according to mass ratio into a reaction vessel with a backflow cooler of a mixer, heating to 80 - 100 DEG C, stirring and reacting for 30 - 50 minutes under the effect of 1 - 3 parts of A type catalyst, then adding 10 parts - 20 parts of B type catalyst and 150 parts - 200 parts of sulfonate to heat at the temperature range of 90 DEG C - 105 DEG C to react for 1 - 2 hours, then adding 50 - 100 parts of aminosilane coupling type high-molecular polymer, and reheating to the temperature range of 90 DEG C - 105 DEG C for continuing the reaction for 2 - 4 hours, and then discharging the material to obtain coupling phenolic resin. According to the invention, when coupling phenolic resin is taken as a fluid loss agent with heat and salinity tolerance used for the drilling fluid, the high-temperature high-pressure filtration loss is reduced by 8 - 15%, the cloud point salinity is raised by 10 - 20% than that of common sulfonation phenolic resin on the key index tests, and the quality of the filter cake is raised so that the filter cake is thin and dense.
Description
Technical field
The present invention relates to polymeric material field, be specifically related to the preparation method of a kind of petroleum drilling industry drilling fluid, be i.e. the drilling fluid preparation method of coupling resol with anti-salt temperature resistance fluid loss agent.
Background technology
Borehole well instability is to influence the principal element that drilling well is carried out smoothly always in the drilling process, and on-the-spot the employing usually to adding fluid loss agent in the drilling fluid addresses this problem.Yet the temperature resistance ability of existing fluid loss agent is generally not high, generally be no more than 160 ℃, prior art mainly adopts sulfonated phenol formaldehyde resin as fluid loss agent, high temperature resistance highly compressed filter loss instability, anti-salt is lower, especially under the situation that geologic framework differs greatly, just need the littler and higher fluid loss agent of salt resistance of filter loss.
Summary of the invention
The objective of the invention is to overcome the deficiency of existing petroleum drilling industry drilling fluid, all preparation methods of enhanced drilling fluid usefulness coupling resol greatly of a kind of anti-salt, temperature resistance and adsorptivity performance are provided with anti-salt temperature resistance fluid loss agent.
In order to achieve the above object, the present invention has adopted following technical scheme: a kind of drilling fluid preparation method of coupling resol, this preparation method is: by the phenol of quality proportioning with 100 parts, the formaldehyde of 60-200 part adds in the reactor of the reflux cooler that has stirrer successively, under the effect of 1-3 part category-A catalyzer, heated 80-100 ℃ of stirring reaction 30-50 minute, add then 10-20 part category-B catalyzer and 150-200 part sulfonate heat 90-105 ℃ the reaction 1-2 hour, the aminosilane coupling family macromolecule polymkeric substance that adds 50-100 part is again heated 90-105 ℃ again and is continued reaction discharging after 2-4 hour, get final product coupling resol.The present invention can further make coupling resol aqua and pulvis is packed sale.
Above-mentioned category-A catalyzer (acid catalyst) is selected from a kind of in hydrochloric acid, tosic acid or the oxalic acid.
Above-mentioned category-B catalyzer (alkali catalyst) is selected from sodium hydroxid, a kind of in magnesium hydroxide or the potassium hydroxide.
Above-mentioned aminosilane coupling family macromolecule polymkeric substance is selected from the N-2-(aminoethyl)-3-aminopropyl trimethoxysilane, N-(β aminoethyl)-γ-aminopropyl methyl-dimethoxy silane or 3-aminopropyl triethoxysilane.
Above-mentioned sulfonate is selected from Sodium Pyrosulfite or vitriolate of tartar.
The present invention also comprises and utilizes the prepared drilling fluid of aforementioned preparation method coupling resol.
Principle of the present invention is: phenol, formaldehyde, sulfonate are reacted the preliminary resol of formation under the effect of catalyzer, adding aminosilane coupling family macromolecule polymkeric substance again reacts again, obtain coupling resol, mainly show as and add after aminosilane coupling family macromolecule polymkeric substance reacts again, the resin that obtains uses key property to strengthen to some extent.After being mainly reflected in adding coupling high molecular polymer in the practical application, inorganic components in the base slurry and organic composition have improved cohesive action and have fallen the filter effect by coupled action.
Beneficial effect of the present invention is: among the present invention, select different aminosilane coupling family macromolecule polymkeric substance, be added in the late phase reaction of resol, by the effect of functional group, molecule coupled together or inlay additionally mutually, play the effect of strengthening the property.Use the coupling resol that this technical recipe produces can be as drilling fluid during with anti-salt temperature resistance fluid loss agent, improve a lot than common sulfonated phenol formaldehyde resin (SMP-II type) in the test of key index, specific as follows: as to test under 180 ℃ temperature: 1, high temperature and high pre ssure filtration reduces 8-15%; 2, the cloud point salinity improves 10-20%; 3, the quality that has improved filter cake makes filter cake thin and fine and close (after adding the coupling high molecular polymer, inorganic components in the base slurry and organic composition be by coupled action, improved cohesive action and fall and filter effect).
Measure according to standard method, the coupling resol of preparation technology's preparation of the present invention is made corresponding aqua and pulvis carries out index determining respectively, testing index sees Table 1:
The coupling resol of table 1 preparation technology's preparation of the present invention is made corresponding aqua and pulvis index.
Above-mentioned coupling resol aqua and pulvis all adopt the sulfonated phenol formaldehyde resin aqua commonly used at present and the preparation method of pulvis to make.
Description of drawings
Fig. 1 is a process flow sheet of the present invention.
Embodiment
Embodiment 1
Technical process according to Fig. 1, by the quality proportioning 100 parts phenol, 130 parts formaldehyde are added in the reactor of the reflux cooler that has stirrer successively, under the effect of 2 parts of hydrochloric acid, heat 100 ℃ of stirring reactions 45 minutes, adding 15 parts of sodium hydroxide and 170 parts of Sodium Pyrosulfites then heats 100 ℃ and reacted 1.5 hours, the N-2-(aminoethyl that adds 75 parts again)-the 3-aminopropyl trimethoxysilane heats 100 ℃ again and continues to react discharging after 3 hours, get final product coupling resol, make aqua respectively again or pulvis is packed.
Embodiment 2
Technical process according to Fig. 1, by the quality proportioning 100 parts phenol, 130 parts formaldehyde are added in the reactor of the reflux cooler that has stirrer successively, under the effect of 2 parts of tosic acid, heat 95 ℃ of stirring reactions 50 minutes, adding 15 parts of sodium hydroxide and 170 parts of Sodium Pyrosulfites then heats 90 ℃ and reacted 2 hours, the N-(β aminoethyl that adds 75 parts again)-γ-aminopropyl methyl-dimethoxy silane heats 100 ℃ again and continues to react discharging after 3 hours, get final product coupling resol, make aqua respectively again or pulvis is packed.
Embodiment 3
Technical process according to Fig. 1, by the quality proportioning 100 parts phenol, 130 parts formaldehyde are added in the reactor of the reflux cooler that has stirrer successively, under the effect of 2 parts of oxalic acid, heat 100 ℃ of stirring reactions 35 minutes, adding 15 parts of sodium hydroxide and 170 parts of Sodium Pyrosulfites then heats 105 ℃ and reacted 2 hours, adding 75 parts 3-aminopropyl triethoxysilane again heats 105 ℃ again and continues to react discharging after 3 hours, get final product coupling resol, make aqua respectively again or pulvis is packed.
Measure according to standard method, the foregoing description gained coupling resol is made corresponding aqua and pulvis carries out the index contrast with sulfonated-pheno-formoldehyde resin (SMP) II type aqua pulvis respectively, the testing index parameter comparison sees Table 2:
Claims (6)
1. a drilling fluid is with the preparation method of coupling resol, it is characterized in that this preparation method is: by the phenol of quality proportioning with 100 parts, the formaldehyde of 60-200 part adds in the reactor of the reflux cooler that has stirrer successively, under the effect of 1-3 part category-A catalyzer, heated 80-100 ℃ of stirring reaction 30-50 minute, add then 10-20 part category-B catalyzer and 150-200 part sulfonate heat 90-105 ℃ the reaction 1-2 hour, the aminosilane coupling family macromolecule polymkeric substance that adds 50-100 part is again heated 90-105 ℃ again and is continued reaction discharging after 2-4 hour, get final product coupling resol, make aqua respectively again or pulvis is packed.
2. drilling fluid according to claim 1 is with the preparation method of coupling resol, it is characterized in that described category-A catalyzer is selected from a kind of in hydrochloric acid, tosic acid or the oxalic acid.
3. drilling fluid according to claim 1 is characterized in that with the preparation method of coupling resol described category-B catalyzer is selected from sodium hydroxid, a kind of in magnesium hydroxide or the potassium hydroxide.
4. drilling fluid according to claim 1 is characterized in that with the preparation method of coupling resol described aminosilane coupling family macromolecule polymkeric substance is selected from the N-2-(aminoethyl)-3-aminopropyl trimethoxysilane, N-(β aminoethyl)-γ-aminopropyl methyl-dimethoxy silane or 3-aminopropyl triethoxysilane.
5. drilling fluid according to claim 1 is characterized in that with the preparation method of coupling resol described sulfonate is selected from Sodium Pyrosulfite or vitriolate of tartar.
6. use the prepared drilling fluid of the preparation method coupling resol of coupling resol as claim 1,2,3,4 or 5 any described drilling fluids.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201110121858A CN102241804B (en) | 2011-05-12 | 2011-05-12 | Preparation method of coupling phenolic resin used for drilling fluid |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102911329A (en) * | 2012-10-31 | 2013-02-06 | 四川国能伟业科技有限公司 | Method for preparing modified sulfonated phenolic resin for drilling fluids |
| CN104140509A (en) * | 2014-07-29 | 2014-11-12 | 四川上之登新材料有限公司 | Preparation method for sulfonated-phenol-formaldehyde resin formed by modifying benzoxazine resin |
| CN104610521A (en) * | 2014-12-30 | 2015-05-13 | 广州市白云化工实业有限公司 | Silane modified phenolic resin and preparation method thereof |
| CN104788634A (en) * | 2015-05-08 | 2015-07-22 | 天津中油渤星工程科技有限公司 | Preparation method of high-temperature-resistant modified sulfonated phenol formaldehyde resin for drilling fluids |
| CN104844776A (en) * | 2015-05-22 | 2015-08-19 | 中国石油化工股份有限公司 | Preparation method of phenolic resin supermolecular aggregate system |
| CN105754062A (en) * | 2016-03-15 | 2016-07-13 | 东北林业大学 | Low-hydroscopicity phenolic resin insulating gel and preparation method thereof |
| CN108084444A (en) * | 2017-12-29 | 2018-05-29 | 四川正蓉实业有限公司 | A kind of preparation method of drilling fluid heat and salinity tolerance phenolic resin class fluid loss additive |
| CN111440348A (en) * | 2020-04-13 | 2020-07-24 | 江苏鼎峰石油科技有限公司 | Preparation method of flake-type high-temperature-resistant self-suspending plugging agent |
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| CN1517374A (en) * | 2003-01-20 | 2004-08-04 | 孙维钧 | Production method of phenol formaldehyde resin used for normal temperature continuous casting and foaming and resin made by said method |
| US20090325090A1 (en) * | 2008-06-30 | 2009-12-31 | Xerox Corporation | Phenolic resin hole blocking layer photoconductors |
| WO2010103088A1 (en) * | 2009-03-13 | 2010-09-16 | Markem-Imaje | Ink composition for continuous deflected jet printing, especially on wet glass |
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2011
- 2011-05-12 CN CN201110121858A patent/CN102241804B/en active Active
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|---|---|---|---|---|
| CN1517374A (en) * | 2003-01-20 | 2004-08-04 | 孙维钧 | Production method of phenol formaldehyde resin used for normal temperature continuous casting and foaming and resin made by said method |
| US20090325090A1 (en) * | 2008-06-30 | 2009-12-31 | Xerox Corporation | Phenolic resin hole blocking layer photoconductors |
| WO2010103088A1 (en) * | 2009-03-13 | 2010-09-16 | Markem-Imaje | Ink composition for continuous deflected jet printing, especially on wet glass |
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| 《西部探矿工程》 20100115 李尧等 高效磺化酚醛树脂的研制及性能评价 43-46 1-6 , 第1期 * |
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Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102911329B (en) * | 2012-10-31 | 2013-12-04 | 四川国能伟业科技有限公司 | Method for preparing modified sulfonated phenolic resin for drilling fluids |
| CN102911329A (en) * | 2012-10-31 | 2013-02-06 | 四川国能伟业科技有限公司 | Method for preparing modified sulfonated phenolic resin for drilling fluids |
| CN104140509B (en) * | 2014-07-29 | 2015-11-04 | 四川上之登新材料有限公司 | A kind of with the sulfonated-pheno-formoldehyde resin preparation method of benzoxazine colophony modification |
| CN104140509A (en) * | 2014-07-29 | 2014-11-12 | 四川上之登新材料有限公司 | Preparation method for sulfonated-phenol-formaldehyde resin formed by modifying benzoxazine resin |
| CN104610521A (en) * | 2014-12-30 | 2015-05-13 | 广州市白云化工实业有限公司 | Silane modified phenolic resin and preparation method thereof |
| CN104788634A (en) * | 2015-05-08 | 2015-07-22 | 天津中油渤星工程科技有限公司 | Preparation method of high-temperature-resistant modified sulfonated phenol formaldehyde resin for drilling fluids |
| CN104788634B (en) * | 2015-05-08 | 2017-11-07 | 天津中油渤星工程科技有限公司 | A kind of preparation method of drilling fluid high temperature resistance modification sulphonation phenolic resin |
| CN104844776A (en) * | 2015-05-22 | 2015-08-19 | 中国石油化工股份有限公司 | Preparation method of phenolic resin supermolecular aggregate system |
| CN104844776B (en) * | 2015-05-22 | 2018-03-06 | 中国石油化工股份有限公司 | A kind of preparation method of phenolic resin supramolecular aggregation system |
| CN105754062A (en) * | 2016-03-15 | 2016-07-13 | 东北林业大学 | Low-hydroscopicity phenolic resin insulating gel and preparation method thereof |
| CN105754062B (en) * | 2016-03-15 | 2018-01-23 | 东北林业大学 | A kind of low water absorbable phenolic resin insulating cement |
| CN108084444A (en) * | 2017-12-29 | 2018-05-29 | 四川正蓉实业有限公司 | A kind of preparation method of drilling fluid heat and salinity tolerance phenolic resin class fluid loss additive |
| CN111440348A (en) * | 2020-04-13 | 2020-07-24 | 江苏鼎峰石油科技有限公司 | Preparation method of flake-type high-temperature-resistant self-suspending plugging agent |
| CN111440348B (en) * | 2020-04-13 | 2022-05-03 | 江苏鼎峰石油科技有限公司 | Preparation method of flake-type high-temperature-resistant self-suspending plugging agent |
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Address after: Section 2, Shenzhen Road East, Guanghan Economic Development Zone, Deyang City, Sichuan Province Patentee after: Sichuan Zhengrong shangzhideng Technology Co.,Ltd. Address before: Section 2, Shenzhen Road East, Guanghan Economic Development Zone, Deyang City, Sichuan Province Patentee before: SICHUAN SHANGZHIDENG NEW MATERIAL Co.,Ltd. |
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Effective date of registration: 20210414 Address after: No.3, section 3, East Shenzhen road, Guanghan City, Deyang City, Sichuan Province Patentee after: SICHUAN ZHENGRONG IND Co.,Ltd. Patentee after: Sichuan Zhengrong shangzhideng Technology Co.,Ltd. Address before: Section 2, Shenzhen Road East, Guanghan Economic Development Zone, Deyang City, Sichuan Province Patentee before: Sichuan Zhengrong shangzhideng Technology Co.,Ltd. |
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Address after: No.3, section 3, East Shenzhen road, Guanghan City, Deyang City, Sichuan Province Patentee after: Sichuan Zhengrong Industrial Co.,Ltd. Patentee after: Sichuan shangzhideng New Material Technology Co., Ltd Address before: No.3, section 3, East Shenzhen road, Guanghan City, Deyang City, Sichuan Province Patentee before: Sichuan Zhengrong Industrial Co.,Ltd. Patentee before: Sichuan Zhengrong shangzhideng Technology Co., Ltd |
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