In situ generation of nano-clay drilling fluid
US-2017275519-A1 · Sep 28, 2017 · US
US10774257B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10774257-B2 |
| Application number | US-201816129177-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 12, 2018 |
| Priority date | Sep 25, 2017 |
| Publication date | Sep 15, 2020 |
| Grant date | Sep 15, 2020 |
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A random copolymer, a preparation method of the random copolymer, a drilling fluid containing the random copolymer. The random copolymer contains structural unit (A) represented by formula (1), structural unit (B) represented by formula (2), structural unit (C) represented by formula (3), and structural unit (D) represented by formula (4) or (5): wherein X is halogen. When the random copolymer is used as a filter loss reducer in a high-calcium drilling fluid, the filter loss of the high-calcium drilling fluid can be reduced.
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The invention claimed is: 1. A random copolymer containing structural unit (A) represented by formula (1), structural unit (B) represented by formula (2), structural unit (C) represented by formula (3), and structural unit (D) represented by formula (4) and/or formula (5), wherein R 1 and R 2 are H or C 1 -C 6 alkyl respectively and independently, and R 3 and R 4 are H or C 1 -C 3 alkyl respectively and independently; wherein R 5 is —O—R— or —NH—R—, wherein R is —C m H 2m —, m=4, 5 or 6, and M 1 is H, NH 4 , Na or K; wherein R 6 is and M 2 -M 6 are H, NH 4 , Na or K respectively and independently; wherein R 7 and R 8 are H or C 1 -C 6 alkyl respectively and independently, R 9 is —C n H 2n —, n is an integer within a range of 2-6, and R 10 is wherein X is halogen. 2. The random copolymer according to claim 1 , wherein an apparent viscosity of aqueous solution of the random copolymer at 1 wt % concentration is 10-40 mPa·s. 3. The random copolymer according to claim 1 , wherein, based on a total weight of the random copolymer, the random copolymer contains 30-50 wt % structural unit (A), 40-60 wt % structural unit (B), 2-10 wt % structural unit (C), and 1-10 wt % structural unit (D). 4. The random copolymer according to claim 3 , wherein the random copolymer contains 35-45 wt % structural unit (A), 45-55 wt % structural unit (B), 3-8 wt % structural unit (C), and 2-6 wt % structural unit (D). 5. The random copolymer according to claim 1 , wherein in the formula (1), R 1 -R 4 is H; in the formula (2), R 5 is —O—C(CH 3 ) 2 —CH 2 — or —NH—C(CH 3 ) 2 —CH 2 —; in the formula (3), R 6 is in the formula (4), R 7 and R 8 are H or methyl respectively and independently, and R 9 is —CH 2 CH 2 —; in the formula (5), X is Cl. 6. A method for preparing a random copolymer comprising: carrying out a copolymerization reaction of monomer (a) represented by formula (6), monomer (b) represented by formula (7), monomer (c) represented by formula (8), and monomer (d) represented by formula (9) and/or formula (10) under nitrogen shielding and in the presence of an initiator, wherein R 1 and R 2 are H or C 1 -C 6 alkyl respectively and independently, and R 3 and R 4 are H or C 1 -C 3 alkyl respectively and independently; wherein R 5 is —O—R— or —NH—R—, wherein R is —C m H 2m —, m=4, 5 or 6; wherein R 6 is wherein R 7 and R 8 are H or C 1 -C 6 alkyl respectively and independently, R 9 is —C n H 2n —, n is an integer within a range of 2-6, and R 10 is wherein X is halogen. 7. The method according to claim 6 , wherein a dose of monomer (a) is 20-50 pbw, a dose of monomer (b) is 40-70 pbw, a dose of monomer (c) is 1-10 pbw, and a dose of monomer (d) is 0.5-8 pbw. 8. The method according to claim 7 , wherein the dose of monomer (a) is 35-42 pbw, the dose of monomer (b) is 45-55 pbw, the dose of monomer (c) is 3-7 pbw, and the dose of monomer (d) is 1-5 pbw. 9. The method according to claim 6 , wherein in formula (6), R 1 -R 4 are H; in formula (7), R 5 is —O—C(CH 3 ) 2 —CH 2 — or —NH—C(CH 3 ) 2 —CH 2 —; in formula (8), R 6 is in formula (9), R 7 and R 8 are H or methyl respectively and independently, and R 9 is —CH 2 CH 2 —; in the formula (10), X is Cl. 10. The method according to claim 6 , wherein the initiator is selected from oxidation-reduction initiators and/or azo initiators. 11. The method according to claim 6 , wherein a doge of the initiator is 0.1-1.6 wt % of the total weight of all monomers. 12. The method according to claim 11 , wherein the dose of the initiator is 0.3-1.5 wt % of the total weight of all monomers. 13. The method according to claim 6 , wherein the method for free radical copolymerization reactions comprises: dissolving monomer (a), monomer (b), monomer (c) and monomer (d) in an alkaline liquor to form a homogeneous mixture, and then charging nitrogen to the homogenous mixture to remove oxygen, and obtain a mixed solution of the monomers; adjusting the temperature of the mixed solution of the monomers to 40° C.−75° C., and adjusting a pH of the mixed solution of the monomers to 5-10; then adding the initiator to initiate the copolymerization reaction and maintaining the copolymerization reaction for 0.2-4 hrs, to obtain a gelatinous product; and pelleting, drying, and pulverizing the gelatinous product. 14. The method according to claim 13 , wherein in the mixed solution of the monomers, a total weight concentration of monomer (a), monomer (b), monomer (c), and monomer (d) is 20-60 wt %. 15. The method according to claim 13 , wherein the drying is carried out at a temperature of 60-120° C. for a duration of 24 - 36 hrs. 16. A drilling fluid containing the random copolymer according to claim 1 , wherein with respect to 100 mL base mud, a dose of the random copolymer is 0.5-4 g.
Amides or imides · CPC title
and containing other heteroatoms, e.g. 2-acrylamido-2-methylpropane sulfonic acid [AMPS] · CPC title
Azo-compounds · CPC title
Aqueous solvent · CPC title
Lubricant additives · CPC title
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