CN109679617B - Solid foam drainage agent composition suitable for ultra-deep gas well, preparation method and application - Google Patents
Solid foam drainage agent composition suitable for ultra-deep gas well, preparation method and application Download PDFInfo
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- CN109679617B CN109679617B CN201710969820.5A CN201710969820A CN109679617B CN 109679617 B CN109679617 B CN 109679617B CN 201710969820 A CN201710969820 A CN 201710969820A CN 109679617 B CN109679617 B CN 109679617B
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- formula
- agent composition
- foam drainage
- hydrocarbyl
- sodium
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- 239000013051 drainage agent Substances 0.000 title claims abstract description 37
- 239000000203 mixture Substances 0.000 title claims abstract description 31
- 239000008259 solid foam Substances 0.000 title claims abstract description 29
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 229920000768 polyamine Polymers 0.000 claims abstract description 59
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 56
- 229920000570 polyether Polymers 0.000 claims abstract description 56
- 150000001875 compounds Chemical class 0.000 claims abstract description 29
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 24
- 238000004519 manufacturing process Methods 0.000 claims abstract description 18
- 239000007787 solid Substances 0.000 claims abstract description 16
- 239000000945 filler Substances 0.000 claims abstract description 12
- 230000002378 acidificating effect Effects 0.000 claims abstract description 11
- 239000000853 adhesive Substances 0.000 claims abstract description 10
- 230000001070 adhesive effect Effects 0.000 claims abstract description 10
- 239000004064 cosurfactant Substances 0.000 claims abstract description 10
- 239000007789 gas Substances 0.000 claims description 42
- -1 hydrocarbyl carboxylates Chemical class 0.000 claims description 27
- 238000006243 chemical reaction Methods 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 125000001183 hydrocarbyl group Chemical group 0.000 claims description 20
- 235000002639 sodium chloride Nutrition 0.000 claims description 19
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 18
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 16
- 229910052783 alkali metal Inorganic materials 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 12
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims description 12
- 239000003054 catalyst Substances 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 10
- 150000003839 salts Chemical class 0.000 claims description 10
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 10
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 8
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 8
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 8
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 8
- 239000004202 carbamide Substances 0.000 claims description 8
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 8
- 239000002904 solvent Substances 0.000 claims description 8
- OHJMTUPIZMNBFR-UHFFFAOYSA-N biuret Chemical compound NC(=O)NC(N)=O OHJMTUPIZMNBFR-UHFFFAOYSA-N 0.000 claims description 7
- 238000006722 reduction reaction Methods 0.000 claims description 7
- 239000002202 Polyethylene glycol Substances 0.000 claims description 6
- 238000001704 evaporation Methods 0.000 claims description 6
- 229920002401 polyacrylamide Polymers 0.000 claims description 6
- 229920001223 polyethylene glycol Polymers 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims description 5
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 claims description 5
- 229910006146 SO3M1 Inorganic materials 0.000 claims description 5
- 150000001340 alkali metals Chemical group 0.000 claims description 5
- 239000003945 anionic surfactant Substances 0.000 claims description 5
- 239000012280 lithium aluminium hydride Substances 0.000 claims description 5
- HELHAJAZNSDZJO-OLXYHTOASA-L sodium L-tartrate Chemical compound [Na+].[Na+].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O HELHAJAZNSDZJO-OLXYHTOASA-L 0.000 claims description 5
- 239000001433 sodium tartrate Substances 0.000 claims description 5
- 229960002167 sodium tartrate Drugs 0.000 claims description 5
- 235000011004 sodium tartrates Nutrition 0.000 claims description 5
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 claims description 4
- 229910019142 PO4 Inorganic materials 0.000 claims description 4
- 229920002472 Starch Polymers 0.000 claims description 4
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 claims description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 4
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims description 4
- 150000001412 amines Chemical class 0.000 claims description 4
- 239000000010 aprotic solvent Substances 0.000 claims description 4
- 239000003093 cationic surfactant Substances 0.000 claims description 4
- 239000001913 cellulose Substances 0.000 claims description 4
- 229920002678 cellulose Polymers 0.000 claims description 4
- GOMCKELMLXHYHH-UHFFFAOYSA-L dipotassium;phthalate Chemical compound [K+].[K+].[O-]C(=O)C1=CC=CC=C1C([O-])=O GOMCKELMLXHYHH-UHFFFAOYSA-L 0.000 claims description 4
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 claims description 4
- LNTHITQWFMADLM-UHFFFAOYSA-N gallic acid Chemical compound OC(=O)C1=CC(O)=C(O)C(O)=C1 LNTHITQWFMADLM-UHFFFAOYSA-N 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 4
- 239000013067 intermediate product Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 235000021317 phosphate Nutrition 0.000 claims description 4
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims description 4
- 125000002572 propoxy group Chemical group [*]OC([H])([H])C(C([H])([H])[H])([H])[H] 0.000 claims description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 4
- 239000011780 sodium chloride Substances 0.000 claims description 4
- 239000008107 starch Substances 0.000 claims description 4
- 235000019698 starch Nutrition 0.000 claims description 4
- 125000000547 substituted alkyl group Chemical group 0.000 claims description 4
- 239000011975 tartaric acid Substances 0.000 claims description 4
- 235000002906 tartaric acid Nutrition 0.000 claims description 4
- 239000002888 zwitterionic surfactant Substances 0.000 claims description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 3
- 239000004375 Dextrin Substances 0.000 claims description 3
- 229920001353 Dextrin Polymers 0.000 claims description 3
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 3
- 239000002585 base Substances 0.000 claims description 3
- 229910021538 borax Inorganic materials 0.000 claims description 3
- FOCAUTSVDIKZOP-UHFFFAOYSA-N chloroacetic acid Chemical class OC(=O)CCl FOCAUTSVDIKZOP-UHFFFAOYSA-N 0.000 claims description 3
- 235000015165 citric acid Nutrition 0.000 claims description 3
- 235000019425 dextrin Nutrition 0.000 claims description 3
- 239000012634 fragment Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 239000001632 sodium acetate Substances 0.000 claims description 3
- 235000017281 sodium acetate Nutrition 0.000 claims description 3
- 235000017550 sodium carbonate Nutrition 0.000 claims description 3
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 3
- BSVBQGMMJUBVOD-UHFFFAOYSA-N trisodium borate Chemical compound [Na+].[Na+].[Na+].[O-]B([O-])[O-] BSVBQGMMJUBVOD-UHFFFAOYSA-N 0.000 claims description 3
- FXKMTSIKHBYZSZ-UHFFFAOYSA-N 2-chloroethanesulfonic acid Chemical class OS(=O)(=O)CCCl FXKMTSIKHBYZSZ-UHFFFAOYSA-N 0.000 claims description 2
- DDLBHIIDBLGOTE-UHFFFAOYSA-N 3-chloro-2-hydroxypropane-1-sulfonic acid Chemical class ClCC(O)CS(O)(=O)=O DDLBHIIDBLGOTE-UHFFFAOYSA-N 0.000 claims description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 2
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-M Formate Chemical compound [O-]C=O BDAGIHXWWSANSR-UHFFFAOYSA-M 0.000 claims description 2
- 229910010084 LiAlH4 Inorganic materials 0.000 claims description 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 2
- 229910000288 alkali metal carbonate Inorganic materials 0.000 claims description 2
- 150000008041 alkali metal carbonates Chemical class 0.000 claims description 2
- 150000008051 alkyl sulfates Chemical class 0.000 claims description 2
- 229940045714 alkyl sulfonate alkylating agent Drugs 0.000 claims description 2
- 238000007112 amidation reaction Methods 0.000 claims description 2
- 150000007942 carboxylates Chemical class 0.000 claims description 2
- 230000021523 carboxylation Effects 0.000 claims description 2
- 238000006473 carboxylation reaction Methods 0.000 claims description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 claims description 2
- 238000006555 catalytic reaction Methods 0.000 claims description 2
- 229940106681 chloroacetic acid Drugs 0.000 claims description 2
- 239000003822 epoxy resin Substances 0.000 claims description 2
- 230000032050 esterification Effects 0.000 claims description 2
- 238000005886 esterification reaction Methods 0.000 claims description 2
- WBJINCZRORDGAQ-UHFFFAOYSA-N ethyl formate Chemical class CCOC=O WBJINCZRORDGAQ-UHFFFAOYSA-N 0.000 claims description 2
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 2
- 229940074391 gallic acid Drugs 0.000 claims description 2
- 235000004515 gallic acid Nutrition 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 150000003951 lactams Chemical class 0.000 claims description 2
- 150000002736 metal compounds Chemical class 0.000 claims description 2
- 229910001507 metal halide Inorganic materials 0.000 claims description 2
- 150000005309 metal halides Chemical class 0.000 claims description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 2
- 239000010452 phosphate Substances 0.000 claims description 2
- 229920000647 polyepoxide Polymers 0.000 claims description 2
- 238000003825 pressing Methods 0.000 claims description 2
- 239000012279 sodium borohydride Substances 0.000 claims description 2
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 2
- 239000001509 sodium citrate Substances 0.000 claims description 2
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 claims description 2
- 235000011083 sodium citrates Nutrition 0.000 claims description 2
- 125000001424 substituent group Chemical group 0.000 claims description 2
- 238000006277 sulfonation reaction Methods 0.000 claims description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 2
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims 1
- 239000006260 foam Substances 0.000 abstract description 58
- 238000007599 discharging Methods 0.000 abstract description 11
- 239000007788 liquid Substances 0.000 abstract description 11
- 238000005201 scrubbing Methods 0.000 abstract description 5
- 238000011049 filling Methods 0.000 abstract description 2
- 239000008258 liquid foam Substances 0.000 abstract description 2
- 239000007921 spray Substances 0.000 abstract description 2
- 238000011084 recovery Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 21
- 239000011734 sodium Substances 0.000 description 16
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 15
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- 238000010992 reflux Methods 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Substances [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 description 8
- 239000002253 acid Substances 0.000 description 7
- 230000032683 aging Effects 0.000 description 7
- 235000011181 potassium carbonates Nutrition 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 239000000654 additive Substances 0.000 description 6
- ZSZFXZHKVNYPLL-UHFFFAOYSA-M sodium;1-hydroxypropane-1-sulfonate Chemical compound [Na+].CCC(O)S([O-])(=O)=O ZSZFXZHKVNYPLL-UHFFFAOYSA-M 0.000 description 6
- 229940125904 compound 1 Drugs 0.000 description 5
- 238000005187 foaming Methods 0.000 description 5
- 230000007935 neutral effect Effects 0.000 description 5
- KQFAFFYKLIBKDE-UHFFFAOYSA-M sodium;ethanesulfonate Chemical compound [Na+].CCS([O-])(=O)=O KQFAFFYKLIBKDE-UHFFFAOYSA-M 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- 229940125782 compound 2 Drugs 0.000 description 4
- 229940126214 compound 3 Drugs 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000005457 ice water Substances 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 238000010907 mechanical stirring Methods 0.000 description 4
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 3
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- UBMXFGVZFUYLSN-UHFFFAOYSA-N azanium;propane-1-sulfonate Chemical compound [NH4+].CCCS([O-])(=O)=O UBMXFGVZFUYLSN-UHFFFAOYSA-N 0.000 description 3
- 230000033558 biomineral tissue development Effects 0.000 description 3
- 239000012267 brine Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 3
- FYGHSUNMUKGBRK-UHFFFAOYSA-N 1,2,3-trimethylbenzene Chemical compound CC1=CC=CC(C)=C1C FYGHSUNMUKGBRK-UHFFFAOYSA-N 0.000 description 2
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical compound CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 description 2
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 2
- 125000000954 2-hydroxyethyl group Chemical group [H]C([*])([H])C([H])([H])O[H] 0.000 description 2
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 2
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 2
- 229910010082 LiAlH Inorganic materials 0.000 description 2
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical compound [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 125000003368 amide group Chemical group 0.000 description 2
- 125000002511 behenyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- BGTOWKSIORTVQH-UHFFFAOYSA-N cyclopentanone Chemical compound O=C1CCCC1 BGTOWKSIORTVQH-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- XIRNKXNNONJFQO-UHFFFAOYSA-N ethyl hexadecanoate Chemical compound CCCCCCCCCCCCCCCC(=O)OCC XIRNKXNNONJFQO-UHFFFAOYSA-N 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 2
- 239000004088 foaming agent Substances 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- QSQLTHHMFHEFIY-UHFFFAOYSA-N methyl behenate Chemical compound CCCCCCCCCCCCCCCCCCCCCC(=O)OC QSQLTHHMFHEFIY-UHFFFAOYSA-N 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 125000000913 palmityl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 239000001508 potassium citrate Substances 0.000 description 2
- 229960002635 potassium citrate Drugs 0.000 description 2
- QEEAPRPFLLJWCF-UHFFFAOYSA-K potassium citrate (anhydrous) Chemical compound [K+].[K+].[K+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O QEEAPRPFLLJWCF-UHFFFAOYSA-K 0.000 description 2
- 235000011082 potassium citrates Nutrition 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- FSSPGSAQUIYDCN-UHFFFAOYSA-N 1,3-Propane sultone Chemical compound O=S1(=O)CCCO1 FSSPGSAQUIYDCN-UHFFFAOYSA-N 0.000 description 1
- CLHYKAZPWIRRRD-UHFFFAOYSA-N 1-hydroxypropane-1-sulfonic acid Chemical compound CCC(O)S(O)(=O)=O CLHYKAZPWIRRRD-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical group [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- AXURXPXGTBQYGB-UHFFFAOYSA-N C1(=CC=CC=C1)S(=O)(=O)O.C(CCCCCCCCCCCCCCC)[Na] Chemical compound C1(=CC=CC=C1)S(=O)(=O)O.C(CCCCCCCCCCCCCCC)[Na] AXURXPXGTBQYGB-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 1
- 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 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- OVXRPXGVKBHGQO-UHFFFAOYSA-N abietic acid methyl ester Natural products C1CC(C(C)C)=CC2=CCC3C(C(=O)OC)(C)CCCC3(C)C21 OVXRPXGVKBHGQO-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 229940077388 benzenesulfonate Drugs 0.000 description 1
- SRSXLGNVWSONIS-UHFFFAOYSA-M benzenesulfonate Chemical compound [O-]S(=O)(=O)C1=CC=CC=C1 SRSXLGNVWSONIS-UHFFFAOYSA-M 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Chemical group BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- MRUAUOIMASANKQ-UHFFFAOYSA-N cocamidopropyl betaine Chemical compound CCCCCCCCCCCC(=O)NCCC[N+](C)(C)CC([O-])=O MRUAUOIMASANKQ-UHFFFAOYSA-N 0.000 description 1
- 229940073507 cocamidopropyl betaine Drugs 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- QYDYPVFESGNLHU-UHFFFAOYSA-N elaidic acid methyl ester Natural products CCCCCCCCC=CCCCCCCCC(=O)OC QYDYPVFESGNLHU-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- CCIVGXIOQKPBKL-UHFFFAOYSA-M ethanesulfonate Chemical compound CCS([O-])(=O)=O CCIVGXIOQKPBKL-UHFFFAOYSA-M 0.000 description 1
- 229940067592 ethyl palmitate Drugs 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000015784 hyperosmotic salinity response Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 229910052740 iodine Chemical group 0.000 description 1
- 239000011630 iodine Chemical group 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 229910052987 metal hydride Inorganic materials 0.000 description 1
- 150000004681 metal hydrides Chemical class 0.000 description 1
- OVXRPXGVKBHGQO-UYWIDEMCSA-N methyl (1r,4ar,4br,10ar)-1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylate Chemical compound C1CC(C(C)C)=CC2=CC[C@H]3[C@@](C(=O)OC)(C)CCC[C@]3(C)[C@H]21 OVXRPXGVKBHGQO-UYWIDEMCSA-N 0.000 description 1
- QYDYPVFESGNLHU-KHPPLWFESA-N methyl oleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC QYDYPVFESGNLHU-KHPPLWFESA-N 0.000 description 1
- 229940073769 methyl oleate Drugs 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- LSHROXHEILXKHM-UHFFFAOYSA-N n'-[2-[2-[2-(2-aminoethylamino)ethylamino]ethylamino]ethyl]ethane-1,2-diamine Chemical compound NCCNCCNCCNCCNCCN LSHROXHEILXKHM-UHFFFAOYSA-N 0.000 description 1
- 125000001624 naphthyl group Chemical group 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- XNLICIUVMPYHGG-UHFFFAOYSA-N pentan-2-one Chemical compound CCCC(C)=O XNLICIUVMPYHGG-UHFFFAOYSA-N 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229910000028 potassium bicarbonate Inorganic materials 0.000 description 1
- 235000015497 potassium bicarbonate Nutrition 0.000 description 1
- 239000011736 potassium bicarbonate Substances 0.000 description 1
- 239000001103 potassium chloride Substances 0.000 description 1
- 235000011164 potassium chloride Nutrition 0.000 description 1
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 description 1
- KCXFHTAICRTXLI-UHFFFAOYSA-N propane-1-sulfonic acid Chemical compound CCCS(O)(=O)=O KCXFHTAICRTXLI-UHFFFAOYSA-N 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- BVIXLMYIFZGRBH-UHFFFAOYSA-M sodium;2-chloroethanesulfonate Chemical compound [Na+].[O-]S(=O)(=O)CCCl BVIXLMYIFZGRBH-UHFFFAOYSA-M 0.000 description 1
- TZLNJNUWVOGZJU-UHFFFAOYSA-M sodium;3-chloro-2-hydroxypropane-1-sulfonate Chemical compound [Na+].ClCC(O)CS([O-])(=O)=O TZLNJNUWVOGZJU-UHFFFAOYSA-M 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000011550 stock solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/584—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/588—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific polymers
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Mining & Mineral Resources (AREA)
- Geology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Geochemistry & Mineralogy (AREA)
- Environmental & Geological Engineering (AREA)
- Polyethers (AREA)
Abstract
The invention relates to a solid foam drainage agent composition suitable for an ultra-deep gas well, a preparation method and application thereof, and mainly solves the problem that the existing foam drainage agent contains H2S、CO2The high-temperature and high-salt resistance in an acidic environment is poor, and the problems of production reduction, even spray stopping and difficult filling of the liquid foam discharging agent caused by liquid loading of a high-temperature and high-salt ultra-deep gas well cannot be solved. The solid foam scrubbing agent composition comprises the following components in parts by mass: (1)1 part of polyamine polyether compound; (2) 0.01-100 parts of cosurfactant; (3) 0.05-1000 parts of solid filler; (4) 0-0.5 parts of adhesive; the polyamine polyether compound has a general molecular formula shown in formula (1): the cosurfactant has at least one of the molecular general formula shown in the formula (2) or the molecular general formula shown in the formula (3), so that the problem is solved well, and the cosurfactant can be used for drainage gas recovery of an acidic high-temperature high-salt ultra-deep gas well.
Description
Technical Field
The invention relates to a solid foam drainage agent composition, a preparation method and application thereof, in particular to a solid foam drainage agent composition suitable for an ultra-deep gas well, a preparation method and application thereof.
Background
With the enhancement of the exploitation strength of the gas field, the water output of the gas field becomes a key problem restricting the normal production of the gas well. Foam drainage gas production is a drainage gas production technology which is rapidly developed at home and abroad in recent years, and has the advantages of simple equipment, convenience in construction, low cost, wide applicable well depth range, no influence on normal production of gas wells and the like. Foam drainage is to inject foam drainage agent into a well through an oil pipe or an oil casing ring, and foam with certain stability is generated under the stirring of airflow. The liquid phase slipped and deposited in the pipe is changed into foam, the relative density of fluid at the lower part in the pipe is changed, and the continuously produced gas phase displacement foam flows out of the shaft, so that the accumulated liquid in the shaft is discharged, and the purposes of water drainage and gas production are achieved.
The development of foam drainage agent since the sixties of the last century is carried out abroad, and surfactants such as sulfonate, benzene sulfonate, alkylphenol polyoxyethylene and the like are mostly selected. At present, a multi-component compound system is mostly adopted in the foam drainage agent for drainage and gas production, and in order to enhance the stability of single foam, auxiliaries such as alkali, alcohol, polymer, alkanolamide and the like are usually added into a formula to form reinforced foam. US7122509 reports a high temperature foam drainage agent formulation, which adopts a research idea of neutralization of anionic surfactant and amine to improve the temperature resistance of the system, and the drainage effect and use concentration are not referred to in the patent. US20120279715 reports a foam fluid for increasing oil yield by recovering gas in a gas well, which is an amido group-containing quaternary ammonium salt surfactant having both foam drainage and sterilization functions, a hydrophobic chain is a hydrophobic segment in substituted naphthalene ring, benzene ring or natural oil ester, and has strong chlorine resistance and condensate oil resistance, and also has good corrosion inhibition performance, the foam agent with an active matter concentration of 400ppm has a foam drainage rate of 86.8% in tap water and a foam drainage rate of 79.1% in simulated brine with a mineralization degree of 130000mg/L, however, because an amide group sensitive to high temperature is contained in a molecular structure, the foam fluid has poor adaptability to gas wells with a temperature of more than 100 ℃. China is a technology for researching foam drainage and gas production processes from the last 80 years, and a patent CN102212348A discloses a salt-resistant and methanol-resistant foam drainage agent, which comprises the following components in percentage by weight: 20-40% of cocamidopropyl betaine, 45-65% of amine oxide, 5-20% of alpha-olefin sulfonate, 5-15% of triethanolamine, 0.2-2% of fluorocarbon surfactant and 0-5% of methanol, wherein the mineralization resistance can reach 18 ten thousand, and the amount of the foaming agent is 5000ppm, but the agent contains the fluorocarbon surfactant, so that not only the cost is greatly improved, but also the environmental impact is large.
The results show that the poor high-temperature and high-salt resistance is a main factor for restricting the development of the foam drainage technology of the high-temperature ultra-deep gas well.
Disclosure of Invention
The invention aims to solve the technical problems that the existing foam drainage agent has poor high-temperature resistance in an acid environment, cannot solve the problems of yield reduction and even spray stopping caused by liquid accumulation of a high-temperature ultra-deep gas well and difficulty in filling a liquid foam drainage agent, and provides a solid foam drainage agent composition suitable for the ultra-deep gas well, which is applied to a high-temperature deep well, has very good temperature resistance under an acid condition, and has strong liquid carrying, foaming and foam stabilizing properties.
The second technical problem to be solved by the present invention is to provide a method for preparing a solid foam drainage agent composition suitable for ultra-deep gas wells, which corresponds to the solution of the first technical problem.
The third technical problem to be solved by the present invention is to provide a solid foam drainage agent composition for ultra-deep gas wells, which corresponds to the solution of one of the above technical problems.
In order to solve one of the above technical problems, the technical scheme adopted by the invention is as follows: the solid foam water discharging agent composition suitable for the ultra-deep gas well comprises the following components in parts by weight:
(1)1 part of polyamine polyether compound;
(2) 0.01-100 parts of cosurfactant;
(3) 0.05-1000 parts of solid filler;
(4) 0-0.5 parts of adhesive;
wherein the polyamine polyether compound has a general molecular formula shown in formula (1):
in the formula (1), R1Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R2、R3、R4Independently selected from H, C1~C5Hydrocarbyl or substituted hydrocarbyl carboxylates, C1~C5Alkyl or substituted alkyl sulfonates, C1~C5Hydrocarbyl or substituted hydrocarbyl phosphates or C1~C5At least one of alkyl sulfate or substituted alkyl sulfate, which is not H at the same time; m is-N (A) CH2CH2-the number of fragments, m ═ 1 to 10; a is a substituent represented by the formula (3); s1, s2 and s3 are addition numbers of propoxy groups PO, s1 is 0-30, s2 is 0-30, s0-30% of 3; r1, r2 and r3 are the addition number of ethoxy EO, r1 is 0-30, r2 is 0-30, r3 is 0-30, and s1+ s2+ m s3 and r1+ r2+ m r3 are not zero at the same time;
in the above technical solution, the cosurfactant is preferably at least one selected from a zwitterionic surfactant, a cationic surfactant and an anionic surfactant; the zwitterionic or cationic surfactant preferably has a general molecular formula shown in formula (2):
in the formula (2), R5Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R6、R7Independently selected from (CH)2)aOH、(CH2)bCH3Or C6H5CH2One of (1), R8Is selected from (CH)2)aOH、(CH2)bCH3、C6H5CH2、(CH2)cOr (CH)2)c(CHOH)d(CH2)eWherein a is any integer from 2 to 4, b is any integer from 0 to 5, c is any integer from 1 to 4, d is any integer from 0 to 3, and e is any integer from 1 to 4; n is the addition number of propoxy groups PO, and n is 0-15; p is the addition number of an ethoxy group EO, and p is 0-30; x-Is selected from OH-Halogen anion, HCO3 -、NO3 -、CH3OSO3 -、CH3COO-、COO-、SO3 -Or OSO3 -One of (1);
the anionic surfactant preferably has a general molecular formula represented by formula (3):
in the formula (3), R9And R10The sum is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, M is selected from hydrogen, alkali metal or of the formula NR11(R12)(R13)(R14) At least one of the groups shown, R11、R12、R13、R14Is independently selected from H, (CH)2)aOH or (CH)2)bCH3Wherein a is any integer of 2-4, and b is any integer of 0-5.
In the above technical solution, the solid filler is at least one of carbonate, bicarbonate, sulfate, phosphate, borate, metal halide, formate, acetate, tartaric acid and salts, citric acid and salts, phthalic acid and salts, gallic acid and salts, urea, biuret, and the like; the adhesive is at least one of dextrin, epoxy resin, polyacrylamide, starch, cellulose, polyethylene glycol and the like.
In the above technical scheme, R1、R5Preferably C8~C24Hydrocarbyl or substituted hydrocarbyl. In the above technical scheme, R2、R3、R4Independently preferably H, CH2COOM1、(CH2)3SO3M1Or CH2(CHOH)CH2SO3M1And is not simultaneously H.
In the above technical scheme, R6、R7Preferably CH3、C2H5、(CH2)2OH or C6H5CH2One kind of (1).
In the above technical scheme, R8Preferably CH3、C2H5、(CH2)2OH or C6H5CH2One of (1); or R8X-Preferably CH2COO-、(CH2)3SO3 -、CH2(CHOH)CH2SO3 -One kind of (1).
In the above technical scheme, R9And R10The sum is preferably C7~C23Hydrocarbyl or substituted hydrocarbyl.
In the above technical scheme, M and M1Independently preferably hydrogen, an alkali metal or a compound of the formula NR11(R12)(R13)(R14) At least one of the groups shown.
In the above technical scheme, R11、R12、R13、R14Preferably H, (CH)2)aOH or (CH)2)bCH3One kind of (1).
In the above technical means, a is preferably 2 to 4, and b is preferably 0 to 5.
In the above-mentioned technical means, m is preferably 1 to 5.
In the technical scheme, n is preferably 0-5; p is 0 to 5.
In the above technical solution, preferably, s1+ s2+ m s3 is 0 to 5, r1+ r2+ m r3 is 0 to 10, and s1+ s2+ m s3 and r1+ r2+ m r3 are not zero at the same time; more preferably, s1+ s2+ m s3 is 1 to 5, and r1+ r2+ m r3 is 1 to 10.
In the above technical solution, the solid filler is preferably at least one of sodium carbonate, sodium bicarbonate, sodium borate, sodium chloride, sodium acetate, tartaric acid, sodium tartrate, citric acid, sodium citrate, potassium phthalate, urea, and biuret.
In the above technical solution, the binder is preferably at least one of polyacrylamide, starch, and polyethylene glycol.
In the technical scheme, the mass ratio of the polyamine polyether compound, the cosurfactant, the solid filler and the adhesive in the solid foam drainage agent is 1: 0.1-10: 0.1-200: 0.01-0.1.
The key active ingredients of the solid foam discharging agent composition of the invention are (1) and (2), and the solid foam discharging agent composition can be obtained by mixing the polyamine polyether compound, the solid filler and the binder according to a required proportion, and is preferably obtained by the following technical scheme for solving two technical problems.
To solve the second technical problem, the invention adopts the following technical scheme: a method for preparing a solid foam drainage agent composition suitable for an ultra-deep gas well, which solves one of the above technical problems, comprises the following steps:
(1) preparation of polyamine polyether compounds
a. Amidation reaction:
r is to be0COOR' and H (NHCH)2CH2)mNH2Mixing the catalyst in a molar ratio of 1: 1-2: 0-0.5, reacting at a reaction temperature of 50-200 ℃ for 3-15 hours while stirring, and evaporating alcohol or water generated by the reaction under normal pressure or reduced pressure to obtain the desired amide compound R0CO(NHCH2CH2)mNH2(ii) a Wherein R is0Is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, R' is selected from H and C1~C8C is 1-10, and the catalyst is at least one selected from alkali metal hydroxide, alkali metal alkoxide and alkali metal carbonate;
b. reduction reaction:
R0CO(NHCH2CH2)mNH2the reduction of the lactam can be carried out by catalytic hydrogenation, heterogeneous catalytic reaction at high temperature and high pressure to generate the corresponding amine, or by the following steps: the R synthesized in the step a0CO(NHCH2CH2)mNH2With metal hydrides H-Y+Reduction in an aprotic solvent to give R0CH2(NHCH2CH2)mNH2. Wherein, Y+Is a metal compound, a metal alkyl compound, a metal amino compound;
c. and (3) polyether esterification:
in the presence of a basic catalyst, the R synthesized in the step b0CH2(NHCH2CH2)mNH2Sequentially reacting with required amount of propylene oxide and ethylene oxide to obtain long-chain polyamine polyether intermediate product
R0CH2{N[(CHCH3CH2O)s3(CH2CH2O)r3H][CH2CH2]}mN[(CHCH3CH2O)s1(CH2CH2O)r1H][CHCH3CH2O)s2(CH2CH2O)r2)H];
d. Carboxylation or sulfonation reaction:
c, reacting the long-chain polyamine polyether intermediate product obtained in the step c with an ionizing reagent and alkali in a solvent according to the molar ratio of 1: 1-5: 1-10 at the reaction temperature of 50-120 ℃ for 3-20 hours to generate polyamine polyether carboxylate or polyamine polyether sulfonate shown in the structural formula (1); the ionizing agent is selected from XR15Y1Or X R'15Y′1At least one of; the base is selected from alkali metal hydroxide or alkali metal alkoxide; y is1And Y'1Is SO3M1Or COON1,M1And N1Is an alkali metal, and X is chlorine, bromine or iodine;
(2) uniformly mixing the polyamine polyether compound synthesized in the step (1), the cosurfactant, the solid filler and the adhesive according to the required mass parts, and then pressing and forming to prepare the solid foam drainage agent composition.
In the above-described aspect, the solid foam drainage agent composition may have a shape of a bar, a ball, or the like.
In the above technical scheme, R in the step a1COOR’、H(NHCH2CH2)mNH2The molar ratio of the catalyst is preferably 1: 1-1.3: 0-0.1.
In the above technical scheme, the catalyst in step a is preferably at least one of sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate.
In the above technical scheme, step b is H-Y+Preferably LiAlH4、LiAlH(OEt)3Or NaBH4At least one of (1).
In the above technical solution, the aprotic solvent in step b is preferably at least one of diethyl ether, tetrahydrofuran, and dioxane.
In the above technical scheme, the long-chain polyamine polyether intermediate in step d: ionizing agent: the molar ratio of the alkali is preferably 1: (1-2): (1-4).
In the above technical scheme, the solvent in the step d is preferably selected from C3~C8Ketone and C6~C9For example, at least one of the group consisting of acetone, butanone, pentanone, benzene, toluene or xylene, trimethylbenzene, ethylbenzene and diethylbenzene.
In the above technical solution, the XR15Y1Or X R'15Y′1Examples of (b) include, but are not limited to, alkali metal salts of chloroacetic acid, alkali metal salts of bromoacetic acid, alkali metal salts of 3-chloro-2-hydroxypropanesulfonic acid, alkali metal salts of 2-chloroethanesulfonic acid, and the like.
The solid foam water-discharging agent composition suitable for the ultra-deep gas well has good compatibility, and can also contain other treating agents commonly used in the field.
In order to solve the third technical problem, the technical scheme adopted by the invention is as follows: the application of the solid foam water drainage agent composition suitable for the ultra-deep gas well in any one of the technical schemes in drainage and gas production of the acidic high-temperature high-salinity ultra-deep gas well.
In the above technical scheme, the application of the foam drainage agent is not particularly limited, and those skilled in the art can apply the foam drainage agent according to the existing drainage and gas production process technology, for example, but not limited to, the high-temperature acid gas-containing gas reservoir is preferred, the formation temperature is 150-200 ℃, the total mineralization of formation brine is 5000-200000 mg/L, and H is2S and CO2The content of (A) is 0-35%.
The long-chain polyamine compound containing stable chemical bonds can avoid hydrolysis under acidic high-temperature and high-salt conditions, maintain the stability of a molecular structure and maintain the foam drainage capability of the foam drainage agent to the maximum extent. The invention relates to a solid foam water discharging agent composition suitable for an ultra-deep gas well, a preparation method and application thereof in water discharging and gas production.
The thermal decomposition temperature of the polyamine polyether compound prepared by the invention is 200 ℃ or above, the polyamine polyether compound is not hydrolyzed or is hydrolyzed in a trace amount in an acidic aqueous solution, and the polyamine polyether compound has good temperature resistance; nonionic fragments and multi-hydrophilic groups in molecules increase the salt resistance on one hand, and increase the amount of bound water and bound water carried by the foaming agent on the other hand, so that the liquid carrying amount of the foam is increased, and the liquid separation is slowed down; secondly, the foam water discharging agent simultaneously has functional groups with opposite electric property of negative and positive, so that the adsorption capacity of the foam agent on a gas-liquid interface is increased, and the formed composition is more efficient; in addition, the molecule contains hetero atoms responding to pH, so that the molecular sieve can be applied to the drainage and gas production process of acidic high-temperature high-salt ultra-deep wells with the temperature of 150 ℃ and above at low concentration.
The key effective components of the foam discharging agent, the solid filler and the adhesive have good compatibility, and the formed solid composition does not influence the foam discharging performance.
In the present invention, the content or concentration of the foam discharging agent refers to the total content or total concentration of the components (1) and (2) in the above technical scheme. By adopting the technical scheme of the invention, the foam performance test of the foam drainage agent is carried out according to SY/T6465-2000 foamer evaluation method for foam drainage and gas production, the foaming height reaches 175mm and the liquid carrying rate reaches 93.9 percent before and after high-temperature aging when 0.02-0.12 percent of the foam drainage agent is in 0-200,000 mg/L salinity brine, and the foam drainage agent has excellent temperature resistance, salt tolerance, foaming and liquid carrying performances in an acidic environment, thereby obtaining better technical effects.
The invention is further illustrated by the following examples.
Detailed Description
In order to better understand the present invention, the following examples are further provided to illustrate the present invention, but the present invention is not limited to the following examples.
[ example 1 ]
(1) Preparation of foam scrubbing agent FMG01
a. A reaction flask equipped with mechanical stirring, thermometer, dropping funnel and atmospheric distillation was charged with 127.6 g (0.55 mol) of pentaethylenehexamine and 1.4 g (0.0 mol)25 mol) of potassium hydroxide solid, slowly dripping 148 g (0.5 mol) of methyl oleate while stirring, reacting at the reaction temperature of 120-160 ℃ for 6 hours, and collecting methanol generated by the reaction to obtain the required amide compound C17H33CO(NHCH2CH2)5NH2The yield thereof was found to be 93.8%.
b. Removing water from a three-neck flask device provided with a reflux condenser tube, a dropping funnel and a thermometer, adding 11.4 g (0.3 mol) of lithium aluminum hydride and 90 ml of dry dioxane, stirring, dispersing and mixing, and dropping 49.6 g (0.1 mol) of C at-10-5 DEG C17H33CO(NHCH2CH2)5NH2The 40 wt% dioxane solution is added dropwise and slowly heated to about 35 ℃ for reaction for 3 hours. Carefully pouring the reaction solution into ice water, and carrying out post-treatment to obtain a long-chain polyamine compound C17H33CH2(NHCH2CH2)5NH2The yield thereof was found to be 89.0%.
c. A pressure reactor equipped with a stirring device was charged with 192.8 g (0.4 mol) of C17H33CH2(NHCH2CH2)5NH24.0 g of potassium hydroxide, 469.8 g (8.1 mol) of propylene oxide and 52.8 g (1.2 mol) of ethylene oxide react sequentially at 140-160 ℃ to obtain the long-chain polyamine polyether compound1(R1=C18H35,m=5,s1+s2+5s3=20,r1+r2+5r3=3,R2=R3=R4H), yield 96.2%.
d. Long-chain polyamine polyether compounds1(R1=C18H35,m=5,s1+s2+5s3=20,r1+r2+5r3=3,R2=R3=R4H)177.4 g (0.1 mol) were mixed with 8.0 g (0.2 mol) of sodium hydroxide, 29.5 g (0.15 mol) of sodium 3-chloro-2-hydroxypropanesulfonate and 300 ml of toluene/benzene (v/v ═ 1) in a four-neck flask equipped with a mechanical stirrer, a thermometer and a reflux condenser, and heated to 90 ℃ for 7 hours. Evaporating the solvent to obtain the long-chain polyamine polyether compound1(R1=C18H35,m=5,s1+s2+5s3=20,r1+r2+5r3=3)Sodium hydroxypropanesulfonate (R)2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remainder H).
e. Long-chain polyamine polyether compound1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g, sodium tartrate 100 g, sodium chloride 90 g and urea 30 g are mixed evenly, 10% cellulose water solution 30 g is added for mixing and then pressed into a rod shape, and the foam drainage rod FMG01 is prepared.
(2) FMG01 was dissolved in deionized water, 100,000mg/L, 200,000mg/L NaCl water, respectively, to make up a 0.3 wt% stock solution of the foam-eliminating agent.
The performances of foaming power, foam stability, liquid carrying capacity and the like of the FMG01 solution are determined according to SY/T6465-2000 evaluation method for foam drainage and gas production foamer, and the results are shown in Table 1.
The experiment is carried out by adopting a pressure-resistant and acid-resistant aging device, and the performances such as foaming power, foam stability, liquid carrying capacity and the like are measured again after aging is carried out for 24 hours at 180 ℃, and the results are shown in table 1.
[ example 2 ]
The same as [ example 1 ] except that in the measurement of FMG01 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid to simulate neutral and acid gas environments, and the results are shown in table 2.
[ example 3 ]
The same as [ example 1 ] except that a long-chain polyamine polyether compound is used1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-50 g, 100 g of sodium sulfate, 50 g of potassium bicarbonate, 30 g of sodium borate and 30 g of biuret are uniformly mixed, 30 g of 5% dextrin water solution is added and uniformly mixed to prepare a foam drainage rod FMG02, and the result is shown in Table 3.
[ example 4 ]
The same as [ example 1 ] except that a long-chain polyamine polyether compound is used1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33SO3Na 50 g, sodium tartrate 100 g, sodium chloride 90 g and urea 30 g are mixed uniformly, and 10% cellulose water solution 30 g is added to be mixed uniformly, so as to prepare a foam drainage rod FMG03, and the results are shown in Table 4.
[ example 5 ]
(1) Preparation of foam scrubbing agent FMG 04:
a. adding 67.0 g (0.65 mol) of diethylenetriamine and 6.9 g (0.05 mol) of potassium carbonate solid into a reaction bottle provided with a mechanical stirring device, a thermometer, a dropping funnel and a normal pressure distillation device, slowly dropping 142.0 g (0.5 mol) of ethyl palmitate while stirring, reacting for 4 hours at the reaction temperature of 120-160 ℃, and collecting ethanol generated by the reaction to obtain the required amide compound C15H31CO(NHCH2CH2)2NH2The yield thereof was found to be 94.5%.
b. After removing water from a three-necked flask equipped with a reflux condenser, a dropping funnel and a thermometer, LiAlH (OEt) was added351 g (0.3 mol) and 120 ml of anhydrous ether are stirred and mixed, and 34.1 g (0.1 mol) of C is dripped into the mixture at the temperature of minus 5 to 5 DEG C15H31CO(NHCH2CH2)2NH2Adding 50 wt% anhydrous ether solution, slowly heating to about 30 deg.C, and reacting for 5 hr. Carefully pouring the reaction solution into ice water, and carrying out post-treatment to obtain a long-chain polyamine compound C15H31CH2(NHCH2CH2)2NH2The yield thereof was found to be 83.4%.
c. A pressure reactor equipped with a stirring device was charged with 130.8 g (0.4 mol) of C15H31CH2(NHCH2CH2)2NH25.2 g of potassium carbonate, 70.8 g (1.22 mol) of propylene oxide and 35.2 g (0.8 mol) of ethylene oxide are sequentially reacted at 140-160 ℃ to obtain the long-chain polyamine polyether compound2(R1=C16H33,m=2,s1+s2+2s3=3,r1+r2+2r3=2,R2=R3=R4H), yield 97.6%.
d. Long-chain polyamine polyether compounds2(R1=C16H33,m=2,s1+s2+2s3=3,r1+r2+2r3=2,R2=R3=R4H)58.9 g (0.1 mol) were mixed with 5.7 g (0.11 mol) of sodium methoxide, 13.4 g (0.11 mol of 1, 3-propanesultone and 100 ml of cyclopentanone in a four-neck flask equipped with a mechanical stirrer, a thermometer and a reflux condenser, and after the addition, the temperature was raised to reflux for 5 hours. Evaporating to remove solvent, adding ammonia water to obtain long-chain polyamine polyether compound2(R1=C16H33Ammonium propanesulfonate (R1 + R2+2R3 ═ 2, s1+ s2+2s3 ═ 3, R1+ R2+2R3 ═ 2)2、R3、R4One of them is CH2CH2CH2SO3NH4And the balance is H).
e. Long-chain polyamine polyether compound2(R1=C16H33Ammonium propanesulfonate 80g, C) with m 2, s1+ s2+2s 3-3, r1+ r2+2r 3-2)16H33OC2H4N+(CH3)2CH2COO-20 g, 100 g of potassium citrate, 60 g of urea and 60 g of biuret are uniformly mixed, 30 g of 1% polyacrylamide aqueous solution is added and uniformly mixed, and the foam drainage rod FMG04 is prepared.
(2) The same as [ example 1 ] except that the aging was carried out at 150 ℃ for 72 hours, the results are shown in Table 5.
[ example 6 ]
The same as [ example 5 ] except that in the measurement of FMG04 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid, neutral and acidic gas environments were simulated, and aging was carried out at 150 ℃ for 72 hours, and the results are shown in table 6.
[ example 7 ]
(1) Preparation of foam scrubbing agent FMG 05:
a. adding 36.0 g (0.6 mol) of ethylenediamine and 13.8 g (0.1 mol) of potassium carbonate solid into a reaction bottle provided with a mechanical stirring device, a thermometer, a dropping funnel and a normal pressure distillation device, slowly dropping 177.0 g (0.5 mol) of methyl behenate under stirring, reacting for 3 hours at the reaction temperature of 120-160 ℃, and collecting methanol generated by the reaction to obtain the required amide compound C21H43CONHCH2CH2NH2The yield thereof was found to be 91.6%.
b. Removing water from a three-neck flask device provided with a reflux condenser tube, a dropping funnel and a thermometer, adding 15.2 g (0.4 mol) of lithium aluminum hydride and 100 ml of dry dioxane, stirring, dispersing and mixing, and dropping 38.2 g (0.1 mol) of C at-10-5 DEG C21H43CONHCH2CH2NH2The 40 wt% dioxane solution is added dropwise and slowly heated to about 35 ℃ for reaction for 3 hours. Carefully pouring the reaction solution into ice water, and carrying out post-treatment to obtain a long-chain polyamine compound C21H43CH2NHCH2CH2NH2The yield thereof was found to be 87.9%.
c. A pressure reactor equipped with a stirring device was charged with 147.2 g (0.4 mol) of C21H43CH2NHCH2CH2NH25.2 g of potassium carbonate and 280.7 g (4.84 mol) of propylene oxide react at 140-160 ℃ to obtain a long-chain polyamine polyether compound3(R1=C22H45,m=1,s1+s2+s3=12,r1+r2+r3=0,R2=R3=R4H), yield 98.1%.
d. Long-chain polyamine polyether compounds3(R1=C22H45,m=1,s1+s2+s3=12,r1+r2+r3=0,R2=R3=R4H)106.4 g (0.1 mol) with 16.8 g (0.3 mol) of potassium hydroxide and 15.9 g (0.12 mol) of chloroacetic acidPotassium and 400 ml of acetone are mixed in a reaction kettle provided with a mechanical stirrer, a thermometer and a reflux condenser tube, and heated to reflux reaction for 10 hours. Evaporating the solvent to obtain the long-chain polyamine polyether compound3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK and the rest is H).
e. Long-chain polyamine polyether compound3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK, the remainder H)15 g, C22H45OC2H4N+(CH2CH2OH)2(CH3)CH2COO-90 g internal olefin sulfonate IOS (C)19~23)30 g, 100 g of sodium sulfate, 100 g of sodium tartrate and 70 g of potassium chloride are mixed uniformly, 60 g of 10% polyethylene glycol is added and mixed uniformly, and the foam drainage rod FMG05 is prepared.
(2) The same as [ example 1 ] except that the aging was carried out at 200 ℃ for 24 hours, the results are shown in Table 7.
[ example 8 ]
The same as [ example 7 ] except that in the measurement of FMG05 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid, neutral and acidic gas environments were simulated, and aging was performed at 200 ℃ for 24 hours, and the results are shown in table 8.
[ example 9 ]
(1) Preparation of foam scrubbing agent FMG 06:
a. adding 36.0 g (0.6 mol) of ethylenediamine and 13.8 g (0.1 mol) of potassium carbonate solid into a reaction bottle provided with a mechanical stirring device, a thermometer, a dropping funnel and a normal pressure distillation device, slowly dropping 158.3 g (0.5 mol) of methyl abietate (formula 3) while stirring, reacting at the reaction temperature of 120-160 ℃ for 8 hours, and collecting methanol generated by the reaction to obtain the required amide compound C19H29CONHCH2CH2NH2The yield thereof was found to be 85.6%.
b. Removing water from a three-neck flask device provided with a reflux condenser tube, a dropping funnel and a thermometer, adding 13.3 g (0.35 mol) of lithium aluminum hydride and 100 ml of dry dioxane, stirring, dispersing and mixing, and dropping 34.4 g (0.1 mol) of C at-10-5 DEG C19H29CONHCH2CH2NH2The 40 wt% dioxane solution is added dropwise and slowly heated to about 35 ℃ for reaction for 5 hours. Carefully pouring the reaction liquid into ice water, and carrying out post-treatment to obtain a rosin polyamine compound C19H29CH2NHCH2CH2NH2The yield thereof was found to be 73.2%.
c. To a pressure reactor equipped with a stirring device was added 132.0 g (0.4 mol) of C19H29CH2NHCH2CH2NH25.0 g of potassium hydroxide and 160.2 g (3.64 mol) of ethylene oxide react at 140-160 ℃ to obtain the rosin polyamine polyether compound4(R1=C20H31,m=1,s1+s2+s3=0,r1+r2+r3=9,R2=R3=R4H), yield 91.4%.
d. Rosin polyamine polyether compounds4(R1=C20H31,m=1,s1+s2+s3=0,r1+r2+r3=9,R2=R3=R4H)72.6 g (0.1 mol) were mixed with 8.0 g (0.2 mol) of sodium hydroxide, 33.3 g (0.2 mol) of sodium 2-chloroethanesulfonate and 100 ml of toluene in a reaction vessel equipped with a mechanical stirrer, a thermometer and a reflux condenser and heated to reflux for 6 hours. Evaporating the solvent to obtain the long-chain polyamine polyether compound4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, remainder H).
e. Long-chain polyamine polyether compound4(R1=C20H31,m=1,s1+s2+s3=0,r1+r2Sodium ethanesulfonate (R) of + R3 ═ 9)2、R3、R4One of them is CH2CH2SO3Na, the rest is H)90 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g of potassium phthalate, 50 g of potassium phthalate, 150 g of biuret and 30 g of 5 percent polyethylene glycol solution are added and mixed evenly to prepare the foam drainage rod FMG 06.
(2) The results are shown in Table 9, as in example 1.
[ example 10 ]
The same as [ example 9 ] except that in the measurement of FMG06 performance, pH was adjusted to 7, 4 and 2 with hydrochloric acid to simulate neutral and acid gas-containing environments, and the results are shown in table 10.
[ example 11 ]
The same as [ example 10 ] except that a long-chain polyamine polyether compound is used4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the rest is H)30 g, C16H33C6H4SO390 g of Na (hexadecyl sodium benzene sulfonate), 30 g of potassium citrate, 50 g of urea, 100 g of potassium carbonate and 60 g of sodium acetate are uniformly mixed, 30 g of 1% polyacrylamide aqueous solution is added and uniformly mixed to prepare a foam drainage rod FMG07, and the result is shown in Table 11.
[ COMPARATIVE EXAMPLE 1 ]
The same as [ example 1 ] except that the long-chain polyamine polyether compounds are used1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)100 g, C16H33OC2H4N+(CH3)3Br-100 g, C16H33SO3K100 g substituted long-chain polyamine polyether compound1(R1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g ", other additives were unchanged to form foam drainage sticks FMG08, FMG09, and FMG10, with simulated water of 100,000mg/LNaCl, the results are shown in table 12.
[ COMPARATIVE EXAMPLE 2 ]
The same as [ example 5 ] except that the long-chain polyamine polyether compounds are used2(R1=C16H33100 g of ammonium propanesulfonate with m ═ 2, s1+ s2+2s3 ═ 3, r1+ r2+2r3 ═ 2), and C16H33OC2H4N+(CH3)2CH2COO-100 g of substituted long-chain polyamine polyether compound2(R1=C16H33Ammonium propanesulfonate 80g, C) with m 2, s1+ s2+2s 3-3, r1+ r2+2r 3-2)16H33OC2H4N+(CH3)2CH2COO-20 grams ", other additives were unchanged to form foam drainage sticks FMG11 and FMG12 with simulated water at 100,000mg/LNaCl, and the results are shown in Table 13.
[ COMPARATIVE EXAMPLE 3 ]
The same as [ example 7 ] except that the long-chain polyamine polyether compound is used3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK, the remainder H)135 g of a substituted long-chain polyamine polyether compound3(R1=C22H45Potassium acetate (R) of m 1, s1+ s2+ s 3-12, R1+ R2+ R3-02、R3、R4One of them is CH2COOK, the remainder H)15 g, C22H45OC2H4N+(CH2CH2OH)2(CH3)CH2COO-90 g internal olefin sulfonate IOS (C)19~23)30 g "of other additives, forming a foam drainage bar FMG13 with simulated water of 100,000mg/LNaCl, the results are shown in Table 13.
[ COMPARATIVE EXAMPLE 4 ]
The same as [ example 9 ] except that the long-chain polyamine polyether compound is used4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the remainder being H)100 g of substituted long-chain polyamine polyether compound4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the rest is H)90 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g ", other additives were unchanged to form a foam drainage stick FMG14 with simulated water at 100,000mg/LNaCl, the results are shown in Table 13.
[ COMPARATIVE EXAMPLE 5 ]
The same as [ example 1 ], except that "C" is used17H33CO(NHCH2CH2)5NH250 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g of "substituted" long-chain polyamine polyether Compound 1 (R)1=C18H35Sodium hydroxypropanesulfonate (R1 + R2+5R3 ═ 3), m ═ 5, s1+ s2+5s3 ═ 20, and R1+ R2+5R3 ═ 32、R3、R4One of them is CH2CH(OH)CH2SO3Na, the rest is H)50 g, C16H33OC2H4N+(CH3)3Br-40 g, C16H33SO3K10 g ", other additives were unchanged to form a foam drainage stick FMG15 with simulated water of 100,000mg/LNaCl, the results are shown in Table 14.
[ COMPARATIVE EXAMPLE 6 ]
The same as [ comparative example 5 ] except that in measuring the FMG15 performance, pH was adjusted to 7 and 4 with hydrochloric acid to simulate neutral and acidic gas environments, and the results are shown in table 15.
[ COMPARATIVE EXAMPLE 7 ]
The same as [ example 9 ], except that "C" is used19H29CONHCH2CH2NH290 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g of a substituted long-chain polyamine polyether compound4(R1=C20H31Sodium ethanesulfonate (R) of m 1, s1+ s2+ s 30, R1+ R2+ R3 92、R3、R4One of them is CH2CH2SO3Na, the rest is H)90 g, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 g of a-olefin sulfonate AOS (C)14~18)5 g ", other additives were unchanged to form a foam drainage stick FMG16 with simulated water at 100,000mg/LNaCl, the results are shown in Table 14.
[ COMPARATIVE EXAMPLE 8 ]
The same as in comparative example 7, except that the pH was adjusted to 2 with hydrochloric acid to simulate a high acid-containing gas atmosphere when measuring the FMG16 performance, the results are shown in table 15.
TABLE 1
TABLE 2
TABLE 3
TABLE 4
TABLE 5
TABLE 6
TABLE 7
TABLE 8
TABLE 9
Watch 10
TABLE 11
TABLE 12
Watch 13
TABLE 14
Watch 15
Claims (9)
1. The solid foam drainage agent composition comprises the following components in parts by weight:
(1)1 part of polyamine polyether compound;
(2) 0.1-10 parts of cosurfactant;
(3) 0.1-200 parts of solid filler;
(4) 0.01-0.1 parts of adhesive;
wherein the polyamine polyether compound has a general molecular formula shown in formula (1):
in the formula (1), R1Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R2、R3、R4Independently selected from H, C1~C5Hydrocarbyl or substituted hydrocarbyl carboxylates, C1~C5Alkyl or substituted alkyl sulfonates, C1~C5Hydrocarbyl or substituted hydrocarbyl phosphates or C1~C5At least one of alkyl sulfate or substituted alkyl sulfate, which is not H at the same time; m is-N (A) CH2CH2-the number of fragments, m ═ 1 to 10; a is a substituent represented by the formula (4); s1, s2 and s3 are the addition number of propoxy groups PO, s1 is 0-30, s2 is 0-30, and s3 is 0-30; r1, r2 and r3 are the addition number of ethoxy EO, r1 is 0-30, r2 is 0-30, r3 is 0-30, and s1+ s2+ m s3 and r1+ r2+ m r3 are not zero at the same time;
the cosurfactant is at least one of a zwitterionic surfactant, a cationic surfactant and an anionic surfactant; the zwitterionic or cationic surfactant has a general molecular formula shown in formula (2):
in the formula (2), R5Is selected from C4~C32One of hydrocarbyl or substituted hydrocarbyl, R6、R7Independently selected from (CH)2)aOH、(CH2)bCH3Or C6H5CH2One of (1), R8Is selected from (CH)2)aOH、(CH2)bCH3、C6H5CH2、(CH2)c、(CH2)c(CHOH)d(CH2)eWherein a is any integer from 2 to 4, b is any integer from 0 to 5, c is any integer from 1 to 4, d is any integer from 0 to 3, and e is any integer from 1 to 4; n is the addition number of propoxy groups PO, and n is 0-15; p is an ethoxy groupThe addition number of EO, p is 0-30; x-Is selected from OH-Halogen anion, HCO3-、NO3 -、CH3OSO3 -、CH3COO-、COO-、SO3 -Or OSO3 -One of (1);
the anionic surfactant has a general molecular formula shown in formula (3):
in the formula (3), R9And R10The sum is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, M is selected from hydrogen, alkali metal or of the formula NR11(R12)(R13)(R14) At least one of the groups shown, R11、R12、R13、R14Is independently selected from H, (CH)2)aOH or (CH)2)bCH3Wherein a is any integer of 2-4, and b is any integer of 0-5.
2. The solid foam drainage agent composition of claim 1, wherein R is1、R5Is C8~C24Hydrocarbyl or substituted hydrocarbyl; r9And R10The sum of C7~C23Hydrocarbyl or substituted hydrocarbyl; r2、R3、R4Is H, CH2COOM1、(CH2)3SO3M1Or CH2(CHOH)CH2SO3M1And is not simultaneously H; r6、R7Is CH3、C2H5、(CH2)2OH or C6H5CH2One of (1); r8Is CH3、C2H5、(CH2)2OH or C6H5CH2Or R is8X-Is CH2COO-、(CH2)3SO3 -、CH2(CHOH)CH2SO3 -One of (1); m is 1-5; s1+ s2+ m s3 is 0-5, r1+ r2+ m r3 is 0-10, and is not zero at the same time; n is 0 to 5, and p is 0 to 5.
3. The solid foam drainage agent composition of claim 2, wherein the M is1Is hydrogen, an alkali metal or of the formula NR11(R12)(R13)(R14) At least one of the groups shown, R11、R12、R13、R14Is independently selected from H, (CH)2)aOH or (CH)2)bCH3Wherein a is any integer of 2-4, and b is any integer of 0-5.
4. The solid foam drainage agent composition of claim 1, wherein the solid filler is at least one of carbonate, bicarbonate, sulfate, phosphate, borate, metal halide, formate, acetate, tartaric acid and salts, citric acid and salts, phthalic acid and salts, gallic acid and salts, urea, biuret; the adhesive is at least one of dextrin, epoxy resin, polyacrylamide, starch, cellulose and polyethylene glycol.
5. The solid foam drainage agent composition of claim 4, wherein the solid filler is at least one of sodium carbonate, sodium bicarbonate, sodium borate, sodium chloride, sodium acetate, tartaric acid, sodium tartrate, citric acid, sodium citrate, potassium phthalate, urea, biuret; the adhesive is at least one of polyacrylamide, starch and polyethylene glycol.
6. A method of making the solid foam drainage agent composition of any of claims 1 to 5, comprising the steps of:
(1) preparation of polyamine polyether compounds
a. Amidation reaction:
r is to be0COOR' and H (NHCH)2CH2)mNH2Mixing the catalysts according to the molar ratio of 1 (1-2) to 0-0.5, reacting for 3-15 hours at the reaction temperature of 50-200 ℃ under stirring, and evaporating alcohol or water generated in the reaction under normal pressure or reduced pressure to obtain the required amide compound R0CO(NHCH2CH2)mNH2(ii) a Wherein R is0Is selected from C3~C31One of hydrocarbyl or substituted hydrocarbyl, R' is selected from H and C1~C8M is 1-10, and the catalyst is at least one selected from alkali metal hydroxide, alkali metal alkoxide and alkali metal carbonate;
b. reduction reaction:
R0CO(NHCH2CH2)mNH2the reduction of the lactam adopts a catalytic hydrogenation method, and generates heterogeneous catalytic reaction at high temperature and high pressure to generate corresponding amine, or adopts the following steps: the R synthesized in the step a0CO(NHCH2CH2)mNH2And H-Y+Reduction in an aprotic solvent to give R0CH2(NHCH2CH2)mNH2(ii) a Wherein H-Y+Is a metal compound, a metal alkyl compound, a metal amino compound;
c. and (3) polyether esterification:
in the presence of a basic catalyst, the R synthesized in the step b0CH2(NHCH2CH2)mNH2Sequentially reacting with required amount of propylene oxide and ethylene oxide to obtain long-chain polyamine polyether intermediate product R0CH2{N[(CHCH3CH2O)s3(CH2CH2O)r3H][CH2CH2]}mN[(CHCH3CH2O)s1(CH2CH2O)r1H][CHCH3CH2O)s2(CH2CH2O)r2)H];
d. Carboxylation or sulfonation reaction:
c, mixing the long-chain polyamine polyether intermediate product obtained in the step c with an ionizing agent and a base in a molar ratio of 1: (1-5): (1-10) reacting in a solvent at 50-120 ℃ for 3-20 hours to generate polyamine polyether carboxylate or polyamine polyether sulfonate shown in the structural formula (1); the ionizing agent is selected from XR15Y1Or XR'15Y′1At least one of; the base is selected from alkali metal hydroxide or alkali metal alkoxide; the XR15Y1Or XR'15Y′1Selected from alkali metal salts of chloroacetic acid, bromoacetic acid, 3-chloro-2-hydroxypropanesulfonic acid, and 2-chloroethanesulfonic acid;
(2) uniformly mixing the polyamine polyether compound synthesized in the step (1), the cosurfactant, the solid filler and the adhesive according to the required parts by mass, and then pressing and forming to prepare the solid foam drainage agent composition.
7. The method of making a solid foam drainage agent composition of claim 6, wherein R is the same as R in step a0COOR’、H(NHCH2CH2)mNH2The molar ratio of the catalyst is (1-1.3) to (0-0.1), and the catalyst is at least one of sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate; step b said H-Y+Is LiAlH4Or NaBH4Wherein the aprotic solvent is at least one of diethyl ether, tetrahydrofuran and dioxane.
8. The method of making a solid foam drainage agent composition of claim 6, wherein the long-chain polyamine polyether intermediate of step d: ionizing agent: the molar ratio of the alkali is 1 to (1-2) to (1-4, and the solvent is selected from C3~C8Ketone and C6~C9At least one aromatic hydrocarbon of (1).
9. The use of the solid foam drainage agent composition of any one of claims 1 to 5 in drainage and gas production of acidic high-temperature high-salinity ultra-deep gas wells.
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