CN1818007B - Production of high-temperature diluent of drilling liquid - Google Patents
Production of high-temperature diluent of drilling liquid Download PDFInfo
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- CN1818007B CN1818007B CN 200610009798 CN200610009798A CN1818007B CN 1818007 B CN1818007 B CN 1818007B CN 200610009798 CN200610009798 CN 200610009798 CN 200610009798 A CN200610009798 A CN 200610009798A CN 1818007 B CN1818007 B CN 1818007B
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- maleic anhydride
- sodium salt
- temperature
- feero
- chromo
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Abstract
Production of high-temperature diluent of drilling fluid is carried out by proportioning styrene-maleic anhydride sodium salt 30~50kg with iron-chromium lignin sulfosalt 50~75kg and water 250~300kg. The process is carried out by adding water 250~300kg into container, heating to 45~55 degrees C, adding styrene-maleic anhydride sodium salt 30~50kg into hot water a, agitating for 10~40mins, dissolving, adding iron-chromium lignin sulfosalt 50~75kg into solution b slowly, agitating and dissolving for 10~40mins. It is convenient and cheap, has excellent high-temperature resisting and diluting performances and no environmental pollution.
Description
Technical field
The invention belongs to and fall mucous preparation, specially refer to a kind of preparation method of high-temperature diluent of drilling liquid.
Background technology
Water-base drilling fluid be a kind of be dispersion medium with water, be the fluid of disperse phase with the pulping clay.In the petroleum drilling construction process, when boring chance pulping mudstone stratum, the continuous aquation of landwaste is distributed to and causes wherein native content to increase in the drilling fluid, simultaneously, constantly raise along with well depth increases formation temperature, cause drilling fluid viscosity high more, required drilling fluid additive high temperature resistance is strong more.High-temperature resistant thinner must still keep good dilution about 200 degrees centigrade; Yin Gaowen does not produce DeR, makes drilling fluid keep good rheological when high temperature, improves drilling speed; prevent the generation of bit freezing and other drilling failure, and the protection oil reservoir improves the hole structure quality.Existing high-temperature resistant thinner is as fluosilicic class, polymer class etc., its cost height.
Summary of the invention
The present invention is intended to overcome the deficiencies in the prior art, has developed a kind of preparation method of high-temperature diluent of drilling liquid.
The preparation method of a kind of high-temperature diluent of drilling liquid of the present invention phenylethylene-maleic anhydride sodium salt 30～50kg, feero-chromo-lignosulfonate 50～75kg, water 250～300kg is formulated, and its concrete operation steps is:
A, in container, add entry 250～300kg, be heated to 45～55 ℃;
B, in the hot water of a, add phenylethylene-maleic anhydride sodium salt 30～50kg, stirred 10～40 minutes, fully dissolve;
C, slowly add feero-chromo-lignosulfonate 50～75kg in the solution of b, stirring and dissolving guaranteed not have caking in 10～40 minutes.
It is strong that a kind of high-temperature diluent of drilling liquid of the present invention preparation has a high temperature resistance, and dilution property is good, advantages such as cost is low, cleanliness without any pollution easy to use.
Embodiment
Embodiment 1
The preparation method of a kind of high-temperature diluent of drilling liquid of the present invention is to be 30～50kg with the phenylethylene-maleic anhydride sodium salt, feero-chromo-lignosulfonate 50～75kg, and water 250～300kg is formulated, and its operation steps is as follows:
A, in container, add entry 250～300kg, be heated to 45～55 ℃;
B, in the hot water of a, add phenylethylene-maleic anhydride sodium salt 30～50kg, stirred 10～40 minutes, fully dissolve,
C, slowly add feero-chromo-lignosulfonate 50～75kg in the solution of b, stirring and dissolving guaranteed not have caking in 10～40 minutes, promptly made the high-temperature diluent of drilling liquid finished product.
Embodiment 2
Its operation steps of the preparation method of a kind of high-temperature diluent of drilling liquid of the present invention is as follows:
A, in container, add 250kg water, be heated to 45～50 ℃;
B, in the hot water of a, add phenylethylene-maleic anhydride sodium salt 30kg, stirred 10～20 minutes, fully dissolve;
C, slowly add feero-chromo-lignosulfonate 50kg in the solution of b, stirring and dissolving guaranteed not have caking in 10～20 minutes, promptly made the high-temperature diluent of drilling liquid finished product.
Embodiment 3
The preparation method of a kind of high-temperature diluent of drilling liquid of the present invention is with phenylethylene-maleic anhydride sodium salt 40kg, feero-chromo-lignosulfonate 60kg, and water 270kg is formulated, and its operation steps is as follows:
A, in container, add entry 270kg, be heated to 50～55 ℃;
B, in the hot water of a, add phenylethylene-maleic anhydride sodium salt 40kg, stirred 15～30 minutes, fully dissolve;
C, slowly add feero-chromo-lignosulfonate 60kg in the solution of b, stirring and dissolving guaranteed not have caking in 20～35 minutes, promptly made the high-temperature diluent of drilling liquid finished product.
Embodiment 4
The preparation method of a kind of high-temperature diluent of drilling liquid of the present invention is with phenylethylene-maleic anhydride sodium salt 50kg, feero-chromo-lignosulfonate 75kg, and water 300kg is formulated, and its operation steps is as follows:
A, in container, add entry 300kg, be heated to 50～55 ℃;
B, in the hot water of a, add phenylethylene-maleic anhydride sodium salt 50kg, stirred 30～40 minutes, fully dissolve;
C, slowly add feero-chromo-lignosulfonate 75kg in the solution of b, stirring and dissolving guaranteed not have caking in 30～40 minutes, promptly made the high-temperature diluent of drilling liquid finished product.
Claims (1)
1. the preparation method of a high-temperature diluent of drilling liquid, be to be that raw material is made mixture aqueous solution with phenylethylene-maleic anhydride sodium salt, feero-chromo-lignosulfonate, it is characterized in that the phenylethylene-maleic anhydride sodium salt is 30～50kg, feero-chromo-lignosulfonate 50～75kg, water 250～300kg; Preparation steps is:
A, in container, add entry 250～300kg, be heated to 45～55 ℃;
B, in the hot water of a, add phenylethylene-maleic anhydride sodium salt 30～50kg, stirred 10～40 minutes, fully dissolve;
C, slowly add feero-chromo-lignosulfonate 50～75kg in the solution of b, stirring and dissolving guaranteed not have caking in 10～40 minutes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610009798 CN1818007B (en) | 2006-03-07 | 2006-03-07 | Production of high-temperature diluent of drilling liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610009798 CN1818007B (en) | 2006-03-07 | 2006-03-07 | Production of high-temperature diluent of drilling liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1818007A CN1818007A (en) | 2006-08-16 |
| CN1818007B true CN1818007B (en) | 2010-05-26 |
Family
ID=36918214
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200610009798 Expired - Fee Related CN1818007B (en) | 2006-03-07 | 2006-03-07 | Production of high-temperature diluent of drilling liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1818007B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3730900A (en) * | 1972-09-25 | 1973-05-01 | Milchem Inc | Composition and process for drilling subterranean wells |
| CN1045989A (en) * | 1990-04-16 | 1990-10-10 | 王�锋 | Well-drilling composition diluent |
| CN1110707A (en) * | 1995-02-11 | 1995-10-25 | 毛伟汉 | Diluent of drilling liquid |
| US6832652B1 (en) * | 2003-08-22 | 2004-12-21 | Bj Services Company | Ultra low density cementitious slurries for use in cementing of oil and gas wells |
-
2006
- 2006-03-07 CN CN 200610009798 patent/CN1818007B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3730900A (en) * | 1972-09-25 | 1973-05-01 | Milchem Inc | Composition and process for drilling subterranean wells |
| CN1045989A (en) * | 1990-04-16 | 1990-10-10 | 王�锋 | Well-drilling composition diluent |
| CN1110707A (en) * | 1995-02-11 | 1995-10-25 | 毛伟汉 | Diluent of drilling liquid |
| US6832652B1 (en) * | 2003-08-22 | 2004-12-21 | Bj Services Company | Ultra low density cementitious slurries for use in cementing of oil and gas wells |
Non-Patent Citations (4)
| Title |
|---|
| 夏俭英，谢一翔.钻井泥浆稀释剂的结构特点及其作用机理.油田化学3 2.1986,3(2),76-82. |
| 夏俭英,谢一翔.钻井泥浆稀释剂的结构特点及其作用机理.油田化学3 2.1986,3(2),76-82. * |
| 王颖然.苯乙烯-顺丁烯二酸酐共聚物的用途及其在流体中的减粘分散作用.精细石油化工10 6.1993,10(6),36-38. |
| 王颖然.苯乙烯-顺丁烯二酸酐共聚物的用途及其在流体中的减粘分散作用.精细石油化工10 6.1993,10(6),36-38. * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1818007A (en) | 2006-08-16 |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Daqing pescean Technology Co. Ltd. Assignor: Xiao Ying Contract record no.: 2011230000013 Denomination of invention: Production of high-temperature diluent of drilling liquid Granted publication date: 20100526 License type: Exclusive License Open date: 20060816 Record date: 20110422 |
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| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100526 Termination date: 20110307 |