CN1350047A - High-temperature viscosity reducer for drilling fluid and its production process - Google Patents
High-temperature viscosity reducer for drilling fluid and its production process Download PDFInfo
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- CN1350047A CN1350047A CN 00131542 CN00131542A CN1350047A CN 1350047 A CN1350047 A CN 1350047A CN 00131542 CN00131542 CN 00131542 CN 00131542 A CN00131542 A CN 00131542A CN 1350047 A CN1350047 A CN 1350047A
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- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
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- Consolidation Of Soil By Introduction Of Solidifying Substances Into Soil (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
Abstract
The high-temp. viscosity-reducing agent for drilling fluid is obtained by adopting the folloiwng steps: heating methyl chlorisilane, modified and water-dissolved polyacrylonitrile, organic tin catalyst and fluorohydrocarbyl siloxane and pressurizing them to make them react to obtain basis liquid, then adding general soil and humic acid and making them react at 150-180 deg.C to obtain the invented silicofluorine high-temp. viscosity-reducing agent. It features high viscosity-reducing efficiency, extensive application, resisting high temp. and can raise drilling speed.
Description
The invention belongs to a kind of oilfield chemistry agent of adding in a kind of drilling fluid, particularly comprehensive viscosity-depression agents such as high temperature resistance, anti-salt, anticalcium.
The energy of oil, this preciousness of Sweet natural gas is imbedded in underground dearly, people want to develop it, just must carry out petroleum prospecting and exploitation, exploration and exploitation all be unable to do without drilling well, when drilling well, be used for bottom-hole cleaning and drilling cuttings is carried to ground or safeguards that the circulating fluid that drill-well operation normally carries out is drilling fluid, for the stable performance that guarantees drilling fluid with adapt to drilling technology requirement under the various situations, must in drilling fluid, add various materials and chemical assistant is the oilfield chemistry agent.Viscosity-depression agent is to be the important oil field chemical agent of major function to realize that the slurry dilution disperses and keeps fluid ideal visco-plasticity, and viscosity-depression agent also claims thinner, subtract thick dose etc.
That uses in drilling engineering at present, mainly contains Weibull sodium (NaT), tannin extract alkali lye, xanthan gum, feero-chromo-lignosulfonate (FCLS) and amphoteric ion polymer (XY27) etc.Viscosity reducing effect under medium and low temperature such as tannate, tannin extract alkali lye is better, and maximum operation (service) temperature can only reach 110-120 ℃, runs into Na
+, Ca
+, Mg
+, etc. meeting saltout and precipitate, be not suitable for salt solution and high calcium drilling fluid.Chromium-iron lignosulfonate and amphoteric resin viscosity reduction heat-resisting ability improve a lot, also can only reach 160-170 ℃, after adding, chromium-iron lignosulfonate causes that pH value descends, drilling fluid is prone to bubble, the back mud cake frictional coefficient of taking care of oneself becomes big, more fatal is that it contains the free hexavalent chromium, toxicity is very big, and environment is polluted.
The objective of the invention is to produce the viscosity-depression agent of excellent combination properties such as a kind of high temperature resistance, anti-salt, anticalcium, make its satisfy greatly drilling technology constantly at a high speed, high-quality strides forward, and expands the needs of layer to ultra deep well, orientation well and ocean and various bad ground.
The present invention is achieved in that the viscosity-depression agent of production is to be added by methyl chlorosilane to fill in the hydrolyzer of deionized water, at 30～50 ℃ of following hydrolysis reaction, hydrolyzate through the neutralization with liquid sodium hydroxide in corrosion-resistant reactor, react 2-3h down at 70～90 ℃ and generate methyl silicon sodium alcoholate, in having the reactor of reflux, add polyacrylonitrile and the organotin catalysts of modification through hydrolysis, in still, drip the methyl sodium alkoxide, add the back and under reflux temperature, react 4-6h, add the hydrofluoric ether radical siloxane, be forced into 0.4-0.7Mpa, keep back flow reaction 1-2h, promptly get high-temperature viscosity reducer fluosilicic multipolymer basis liquid; As soil and humic acids drying, pulverizing, join in the glass lined reaction vessel in the ratio of basic liquid measure 30-50%, react 1-3h down at 150-180 ℃ and promptly get drilling fluid fluosilicic high-temperature viscosity reducer.
The present invention has following characteristics: (1) use range is wide, all can normally use when temperature is-15～+ 260 ℃; (2) viscosity break ratio height, viscosity break ratio reaches 95% under this viscosity-depression agent normal temperature by experiment, reaches 87%, 260 ℃ after aging at 180 ℃ and reaches 75% after aging; (3) it also has the special-effect of high temperature resistance, anti-salt, anticalcium; (4) consumption is few, maintenance intervals is long, improves power auger speed, comprehensive cost is low, distinguishing features such as nontoxic non-environmental-pollution.
The present invention is achieved in that the methyl chlorosilane adding fills in the hydrolyzer of deionized water, at 40 ℃ of following hydrolysis reaction, hydrolyzate through the neutralization with liquid sodium hydroxide in corrosion-resistant reactor, react 2.5h down at 80 ℃ and generate methyl silicon sodium alcoholate, in having the reactor of reflux, add polyacrylonitrile and the organotin catalysts of modification through hydrolysis, in still, drip the methyl sodium alkoxide, add the back and under reflux temperature, react 5h, add the hydrofluoric ether radical siloxane, be forced into 0.5Mpa, keep back flow reaction 1.5h, promptly get high-temperature viscosity reducer fluosilicic multipolymer basis liquid; As soil and humic acids drying, pulverizing, join in the glass lined reaction vessel in the ratio of basic liquid measure 40%, react 2h down at 160 ℃ and promptly get drilling fluid fluosilicic high-temperature viscosity reducer.
Claims (2)
1, Drilling fluid high temperature reducing adhesion agent and its preparation method, it is characterized in that: the methyl chlorosilane adding fills in the hydrolyzer of deionized water, at 30～50 ℃ of following hydrolysis reaction, hydrolyzate through the neutralization with liquid sodium hydroxide in corrosion-resistant reactor, react 2-3h down at 70～90 ℃ and generate methyl silicon sodium alcoholate, in having the reactor of reflux, add modification through water-soluble polyacrylonitrile and organotin catalysts, in still, drip the methyl sodium alkoxide, add the back and under reflux temperature, react 4-6h, add the hydrofluoric ether radical siloxane, be forced into 0.4-0.7Mpa, keep back flow reaction 1-2h, promptly get high-temperature viscosity reducer fluosilicic multipolymer basis liquid; As soil and humic acids drying, pulverizing, join in the glass lined reaction vessel in the ratio of basic liquid measure 30-50%, react 1-3h down at 150-180 ℃ and promptly get high-temperature viscosity reducer.
2, viscosity-depression agent according to claim 1 is characterized in that: the methyl chlorosilane adding fills in the hydrolyzer of deionized water, at 40 ℃ of following hydrolysis reaction, hydrolyzate through the neutralization with liquid sodium hydroxide in corrosion-resistant reactor, react 2.5h down at 80 ℃ and generate methyl silicon sodium alcoholate, in having the reactor of reflux, add polyacrylonitrile and the organotin catalysts of modification through hydrolysis, in still, drip the methyl sodium alkoxide, add the back and under reflux temperature, react 5h, add the hydrofluoric ether radical siloxane, be forced into 0.5Mpa, keep back flow reaction 1.5h, promptly get high-temperature viscosity reducer fluosilicic multipolymer basis liquid; As soil and humic acids drying, pulverizing, join in the glass lined reaction vessel in the ratio of basic liquid measure 40%, react 2h down at 160 ℃ and promptly get drilling fluid fluosilicic high-temperature viscosity reducer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB001315420A CN1165594C (en) | 2000-10-25 | 2000-10-25 | High-temperature viscosity reducer for drilling fluid and its production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB001315420A CN1165594C (en) | 2000-10-25 | 2000-10-25 | High-temperature viscosity reducer for drilling fluid and its production process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1350047A true CN1350047A (en) | 2002-05-22 |
| CN1165594C CN1165594C (en) | 2004-09-08 |
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|---|---|---|---|
| CNB001315420A Expired - Lifetime CN1165594C (en) | 2000-10-25 | 2000-10-25 | High-temperature viscosity reducer for drilling fluid and its production process |
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Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100436564C (en) * | 2005-12-22 | 2008-11-26 | 新疆三精德润科技有限公司 | Temperature-resistant viscosity-reducing agent for boring fluid |
| CN102311725A (en) * | 2011-06-29 | 2012-01-11 | 陆明富 | Preparation method for organosilicon viscosity reducer used for drilling fluid |
| CN102352005A (en) * | 2011-07-29 | 2012-02-15 | 山东高唐科林环保科技有限公司 | Process for producing bore drilling fluid additive by utilizing paper-making waste liquid |
| CN102408888A (en) * | 2010-09-21 | 2012-04-11 | 中国石油天然气集团公司 | Rock breaking drilling fluid |
| CN105199059A (en) * | 2015-10-29 | 2015-12-30 | 中国地质大学（北京） | Chromium-free viscosity reducer for drilling fluid for oil field and preparation method of viscosity reducer |
| CN105349119A (en) * | 2015-12-02 | 2016-02-24 | 中国石油集团川庆钻探工程有限公司 | Preparation method of cationic silicofluoride diluent for drilling fluid |
| CN105647501A (en) * | 2016-02-29 | 2016-06-08 | 扬州润达油田化学剂有限公司 | Viscosity reducer for drilling fluid and preparation method of viscosity reducer |
| CN106753284A (en) * | 2017-01-05 | 2017-05-31 | 中国科学院化学研究所 | A kind of viscosity reducer for crude oil and preparation method thereof |
| CN106833555A (en) * | 2017-01-24 | 2017-06-13 | 福州大学 | Method and its application of high-efficient drilling fluid thinner are prepared using percolate |
| CN109181657A (en) * | 2018-09-20 | 2019-01-11 | 河北硅谷化工有限公司 | Drilling fluid anti-collapse and anti-falling filtration agent |
| CN110628406A (en) * | 2019-09-26 | 2019-12-31 | 天津龙净环保科技有限公司 | Thick oil viscosity reducer and production equipment thereof |
| CN111718784A (en) * | 2020-07-25 | 2020-09-29 | 淮北金岭石化有限公司 | Preparation process of emulsified oil complexing agent for hydraulic support |
| CN116463114A (en) * | 2023-03-20 | 2023-07-21 | 山东海嘉石油化工有限公司 | Preparation method and application of thickened oil viscosity reducer |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100362077C (en) * | 2005-12-27 | 2008-01-16 | 宋福如 | Silicon fluorine anti-falldown filter agent for drilling fluid |
-
2000
- 2000-10-25 CN CNB001315420A patent/CN1165594C/en not_active Expired - Lifetime
Cited By (19)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100436564C (en) * | 2005-12-22 | 2008-11-26 | 新疆三精德润科技有限公司 | Temperature-resistant viscosity-reducing agent for boring fluid |
| CN102408888A (en) * | 2010-09-21 | 2012-04-11 | 中国石油天然气集团公司 | Rock breaking drilling fluid |
| CN102408888B (en) * | 2010-09-21 | 2013-07-03 | 中国石油天然气集团公司 | Rock breaking drilling fluid |
| CN102311725A (en) * | 2011-06-29 | 2012-01-11 | 陆明富 | Preparation method for organosilicon viscosity reducer used for drilling fluid |
| CN102352005A (en) * | 2011-07-29 | 2012-02-15 | 山东高唐科林环保科技有限公司 | Process for producing bore drilling fluid additive by utilizing paper-making waste liquid |
| CN102352005B (en) * | 2011-07-29 | 2013-07-17 | 山东高唐科林环保科技有限公司 | Process for producing bore drilling fluid additive by utilizing paper-making waste liquid |
| CN105199059A (en) * | 2015-10-29 | 2015-12-30 | 中国地质大学（北京） | Chromium-free viscosity reducer for drilling fluid for oil field and preparation method of viscosity reducer |
| CN105349119B (en) * | 2015-12-02 | 2017-12-05 | 中国石油集团川庆钻探工程有限公司 | Preparation method of silicofluoride diluent for drilling fluid |
| CN105349119A (en) * | 2015-12-02 | 2016-02-24 | 中国石油集团川庆钻探工程有限公司 | Preparation method of cationic silicofluoride diluent for drilling fluid |
| CN105647501A (en) * | 2016-02-29 | 2016-06-08 | 扬州润达油田化学剂有限公司 | Viscosity reducer for drilling fluid and preparation method of viscosity reducer |
| CN105647501B (en) * | 2016-02-29 | 2018-04-24 | 扬州润达油田化学剂有限公司 | Viscosity depressant for drilling fluid and preparation method thereof |
| CN106753284A (en) * | 2017-01-05 | 2017-05-31 | 中国科学院化学研究所 | A kind of viscosity reducer for crude oil and preparation method thereof |
| CN106753284B (en) * | 2017-01-05 | 2019-03-19 | 中国科学院化学研究所 | A kind of viscosity reducer for crude oil and preparation method thereof |
| CN106833555A (en) * | 2017-01-24 | 2017-06-13 | 福州大学 | Method and its application of high-efficient drilling fluid thinner are prepared using percolate |
| CN106833555B (en) * | 2017-01-24 | 2019-05-31 | 福州大学 | The method and its application of drilling fluid thinner are prepared using landfill leachate |
| CN109181657A (en) * | 2018-09-20 | 2019-01-11 | 河北硅谷化工有限公司 | Drilling fluid anti-collapse and anti-falling filtration agent |
| CN110628406A (en) * | 2019-09-26 | 2019-12-31 | 天津龙净环保科技有限公司 | Thick oil viscosity reducer and production equipment thereof |
| CN111718784A (en) * | 2020-07-25 | 2020-09-29 | 淮北金岭石化有限公司 | Preparation process of emulsified oil complexing agent for hydraulic support |
| CN116463114A (en) * | 2023-03-20 | 2023-07-21 | 山东海嘉石油化工有限公司 | Preparation method and application of thickened oil viscosity reducer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1165594C (en) | 2004-09-08 |
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Assignee: Nanjing Aoshun Electric Power Technology Development Co., Ltd. Assignor: Song Furu Contract fulfillment period: 2009.4.1 to 2015.4.1 Contract record no.: 2009320000813 Denomination of invention: High-temperature viscosity reducer for drilling fluid and its production process Granted publication date: 20040908 License type: Exclusive license Record date: 20090511 |
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| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.4.1 TO 2015.4.1; CHANGE OF CONTRACT Name of requester: NANJING AOSHUN POWER SCIENCE DEVELOPMENT CO., LTD. Effective date: 20090511 |
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Granted publication date: 20040908 |
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