CN109679615A - The method that ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition - Google Patents
The method that ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition Download PDFInfo
- Publication number
- CN109679615A CN109679615A CN201710969702.4A CN201710969702A CN109679615A CN 109679615 A CN109679615 A CN 109679615A CN 201710969702 A CN201710969702 A CN 201710969702A CN 109679615 A CN109679615 A CN 109679615A
- Authority
- CN
- China
- Prior art keywords
- water discharge
- agent composition
- discharge agent
- foaming
- foaming water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 133
- 238000005187 foaming Methods 0.000 title claims abstract description 83
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 81
- 239000000203 mixture Substances 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 25
- 238000005086 pumping Methods 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- 229920000768 polyamine Polymers 0.000 claims abstract description 57
- 229920000570 polyether Polymers 0.000 claims abstract description 52
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 44
- 239000000243 solution Substances 0.000 claims abstract description 26
- 150000001875 compounds Chemical class 0.000 claims abstract description 16
- 150000003839 salts Chemical class 0.000 claims abstract description 12
- 235000019198 oils Nutrition 0.000 claims abstract description 11
- 239000004064 cosurfactant Substances 0.000 claims abstract description 9
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 7
- 238000006073 displacement reaction Methods 0.000 claims abstract description 4
- 239000012530 fluid Substances 0.000 claims abstract description 4
- 239000011259 mixed solution Substances 0.000 claims abstract description 4
- 235000019476 oil-water mixture Nutrition 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 66
- -1 hydrocarbon radical Chemical class 0.000 claims description 39
- 238000006243 chemical reaction Methods 0.000 claims description 35
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 21
- 239000004215 Carbon black (E152) Substances 0.000 claims description 18
- 229930195733 hydrocarbon Natural products 0.000 claims description 18
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 16
- 229910052783 alkali metal Inorganic materials 0.000 claims description 14
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 11
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 150000001340 alkali metals Chemical class 0.000 claims description 10
- 125000000217 alkyl group Chemical group 0.000 claims description 10
- 239000003054 catalyst Substances 0.000 claims description 10
- 239000003921 oil Substances 0.000 claims description 10
- 239000003513 alkali Substances 0.000 claims description 9
- 238000006722 reduction reaction Methods 0.000 claims description 9
- 239000002904 solvent Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 9
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 claims description 8
- 238000002360 preparation method Methods 0.000 claims description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 7
- 229910006146 SO3M1 Inorganic materials 0.000 claims description 6
- 239000002253 acid Substances 0.000 claims description 6
- 239000003153 chemical reaction reagent Substances 0.000 claims description 6
- 239000013067 intermediate product Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 150000001408 amides Chemical class 0.000 claims description 5
- 229910052739 hydrogen Inorganic materials 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 5
- 239000012280 lithium aluminium hydride Substances 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 claims description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 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
- 239000003945 anionic surfactant Substances 0.000 claims description 4
- 239000003093 cationic surfactant Substances 0.000 claims description 4
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 claims description 4
- 239000002563 ionic surfactant Substances 0.000 claims description 4
- 150000002500 ions Chemical class 0.000 claims description 4
- 239000003350 kerosene Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 239000003345 natural gas Substances 0.000 claims description 4
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 3
- 229910010082 LiAlH Inorganic materials 0.000 claims description 3
- 239000000010 aprotic solvent Substances 0.000 claims description 3
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Chemical group BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052794 bromium Inorganic materials 0.000 claims description 3
- 230000021523 carboxylation Effects 0.000 claims description 3
- 238000006473 carboxylation reaction Methods 0.000 claims description 3
- 239000000460 chlorine Substances 0.000 claims description 3
- 229910052801 chlorine Inorganic materials 0.000 claims description 3
- 150000002430 hydrocarbons Chemical class 0.000 claims description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical group [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 2
- 229910010084 LiAlH4 Inorganic materials 0.000 claims description 2
- 238000011938 amidation process Methods 0.000 claims description 2
- 239000012267 brine Substances 0.000 claims description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 claims description 2
- 125000001309 chloro group Chemical group Cl* 0.000 claims description 2
- 239000010779 crude oil Substances 0.000 claims description 2
- 238000006266 etherification reaction Methods 0.000 claims description 2
- 125000000816 ethylene group Chemical group [H]C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 229910000765 intermetallic Inorganic materials 0.000 claims description 2
- 229910052740 iodine Chemical group 0.000 claims description 2
- 239000011630 iodine Chemical group 0.000 claims description 2
- 229910052987 metal hydride Inorganic materials 0.000 claims description 2
- 150000004681 metal hydrides Chemical class 0.000 claims description 2
- 239000012279 sodium borohydride Substances 0.000 claims description 2
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 claims description 2
- 125000001424 substituent group Chemical group 0.000 claims description 2
- 238000003786 synthesis reaction Methods 0.000 claims description 2
- 150000002431 hydrogen Chemical class 0.000 claims 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims 1
- 229940126062 Compound A Drugs 0.000 claims 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims 1
- NLDMNSXOCDLTTB-UHFFFAOYSA-N Heterophylliin A Natural products O1C2COC(=O)C3=CC(O)=C(O)C(O)=C3C3=C(O)C(O)=C(O)C=C3C(=O)OC2C(OC(=O)C=2C=C(O)C(O)=C(O)C=2)C(O)C1OC(=O)C1=CC(O)=C(O)C(O)=C1 NLDMNSXOCDLTTB-UHFFFAOYSA-N 0.000 claims 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 229910019142 PO4 Inorganic materials 0.000 claims 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 claims 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims 1
- 239000003245 coal Substances 0.000 claims 1
- 150000002240 furans Chemical class 0.000 claims 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims 1
- 239000010931 gold Substances 0.000 claims 1
- 229910052737 gold Inorganic materials 0.000 claims 1
- 238000007210 heterogeneous catalysis Methods 0.000 claims 1
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims 1
- 239000010452 phosphate Substances 0.000 claims 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 claims 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims 1
- 229910001948 sodium oxide Inorganic materials 0.000 claims 1
- 230000002378 acidificating effect Effects 0.000 abstract description 7
- 241000521257 Hydrops Species 0.000 abstract description 3
- 206010030113 Oedema Diseases 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract description 2
- 235000020681 well water Nutrition 0.000 abstract description 2
- 239000002349 well water Substances 0.000 abstract description 2
- 239000006260 foam Substances 0.000 description 29
- 239000011734 sodium Substances 0.000 description 18
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 15
- 239000007788 liquid Substances 0.000 description 14
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- 238000004088 simulation Methods 0.000 description 12
- 230000032683 aging Effects 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 10
- 238000007599 discharging Methods 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 238000010907 mechanical stirring Methods 0.000 description 8
- 238000010992 reflux Methods 0.000 description 8
- 238000005259 measurement Methods 0.000 description 7
- 238000006467 substitution reaction Methods 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- 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 6
- 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 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 5
- NGSFWBMYFKHRBD-UHFFFAOYSA-M sodium lactate Chemical compound [Na+].CC(O)C([O-])=O NGSFWBMYFKHRBD-UHFFFAOYSA-M 0.000 description 5
- 239000004094 surface-active agent Substances 0.000 description 5
- 238000010792 warming Methods 0.000 description 5
- 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 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 4
- 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 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 238000004821 distillation Methods 0.000 description 4
- QDPMLKBAQOZXEF-UHFFFAOYSA-N ethanesulfonic acid;sodium Chemical compound [Na].CCS(O)(=O)=O QDPMLKBAQOZXEF-UHFFFAOYSA-N 0.000 description 4
- 239000005457 ice water Substances 0.000 description 4
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 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 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 238000003483 aging Methods 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
- 230000000694 effects Effects 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- 239000004088 foaming agent Substances 0.000 description 3
- 229940072033 potash Drugs 0.000 description 3
- 235000015320 potassium carbonate Nutrition 0.000 description 3
- 235000011181 potassium carbonates Nutrition 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 230000000087 stabilizing effect Effects 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
- 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
- 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 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000002585 base Substances 0.000 description 2
- 150000007942 carboxylates Chemical class 0.000 description 2
- BGTOWKSIORTVQH-UHFFFAOYSA-N cyclopentanone Chemical compound O=C1CCCC1 BGTOWKSIORTVQH-UHFFFAOYSA-N 0.000 description 2
- 239000008367 deionised water Substances 0.000 description 2
- 229910021641 deionized water Inorganic materials 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000005516 engineering process Methods 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
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000012452 mother liquor Substances 0.000 description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 235000011056 potassium acetate Nutrition 0.000 description 2
- KCXFHTAICRTXLI-UHFFFAOYSA-N propane-1-sulfonic acid Chemical compound CCCS(O)(=O)=O KCXFHTAICRTXLI-UHFFFAOYSA-N 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 description 2
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N 1,2-diethylbenzene Chemical group CCC1=CC=CC=C1CC KVNYFPKFSJIPBJ-UHFFFAOYSA-N 0.000 description 1
- JYTNGEWJAZCVAN-UHFFFAOYSA-N 2-hexadecylbenzenesulfonic acid;sodium Chemical compound [Na].CCCCCCCCCCCCCCCCC1=CC=CC=C1S(O)(=O)=O JYTNGEWJAZCVAN-UHFFFAOYSA-N 0.000 description 1
- ALRHLSYJTWAHJZ-UHFFFAOYSA-M 3-hydroxypropionate Chemical group OCCC([O-])=O ALRHLSYJTWAHJZ-UHFFFAOYSA-M 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-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
- 239000004593 Epoxy Substances 0.000 description 1
- 101000892326 Homo sapiens Transmembrane protein 184B Proteins 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical class [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 description 1
- 102100040670 Transmembrane protein 184B Human genes 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- NDQKGYXNMLOECO-UHFFFAOYSA-N acetic acid;potassium Chemical compound [K].CC(O)=O NDQKGYXNMLOECO-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 239000003146 anticoagulant agent Substances 0.000 description 1
- 229940127219 anticoagulant drug Drugs 0.000 description 1
- 239000012752 auxiliary agent Substances 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
- 229940077388 benzenesulfonate Drugs 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 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
- 229940125904 compound 1 Drugs 0.000 description 1
- 239000012141 concentrate Substances 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
- 239000006071 cream Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010586 diagram 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
- 230000002708 enhancing effect Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 229940067592 ethyl palmitate Drugs 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000003672 gas field water Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 125000005842 heteroatom Chemical group 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 150000004702 methyl esters Chemical class 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
- 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
- 150000002790 naphthalenes Chemical class 0.000 description 1
- XNLICIUVMPYHGG-UHFFFAOYSA-N pentan-2-one Chemical compound CCCC(C)=O XNLICIUVMPYHGG-UHFFFAOYSA-N 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 125000002467 phosphate group Chemical class [H]OP(=O)(O[H])O[*] 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- KPFSGNRRZMYZPH-UHFFFAOYSA-M potassium;2-chloroacetate Chemical class [K+].[O-]C(=O)CCl KPFSGNRRZMYZPH-UHFFFAOYSA-M 0.000 description 1
- LVTJOONKWUXEFR-FZRMHRINSA-N protoneodioscin Natural products O(C[C@@H](CC[C@]1(O)[C@H](C)[C@@H]2[C@]3(C)[C@H]([C@H]4[C@@H]([C@]5(C)C(=CC4)C[C@@H](O[C@@H]4[C@H](O[C@H]6[C@@H](O)[C@@H](O)[C@@H](O)[C@H](C)O6)[C@@H](O)[C@H](O[C@H]6[C@@H](O)[C@@H](O)[C@@H](O)[C@H](C)O6)[C@H](CO)O4)CC5)CC3)C[C@@H]2O1)C)[C@H]1[C@H](O)[C@H](O)[C@H](O)[C@@H](CO)O1 LVTJOONKWUXEFR-FZRMHRINSA-N 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 150000008053 sultones Chemical class 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000012085 test solution Substances 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 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)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- Geochemistry & Mineralogy (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The present invention relates to a kind of methods that ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition, mainly solve existing foaming water discharge agent containing H2S、CO2Resisting high temperature, high salt performance is poor under acidic environment, and high temperature and high salt ultra-deep gas well can not be solved the problems, such as because of the underproduction even stop-spraying caused by hydrops.The present invention is by using the following steps are included: foaming water discharge agent composition and water are mixed to get foaming water discharge agent composition solution by (1)；(2) mixed solution of foaming water discharge agent composition solution or foaming water discharge agent composition solution and oil is come into full contact with gas, formation aerated fluid, by the foaming water discharge agent composition solution water or oil water mixture displacement come out；The foaming water discharge agent composition is in terms of mass fraction including following components: 1) 1 part of polyamines polyether compound；2) technical solution of 0.01~100 portion of cosurfactant preferably resolves the problem, can be used in acidic high-temperature ultra-deep gas well water pumping gas production with high salt.
Description
Technical field
The present invention relates to a kind of methods that ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition.
Background technique
With the reinforcement of gas-field exploitation dynamics, gas field is discharged the critical issue normally produced at gas well is restricted.Foam row
Hydromining gas is a kind of drainage gas recovery that recent domestic rapidly develops, simple, easy for construction, at low cost with equipment,
Applicable well depth range is big, does not influence the advantages that gas well normally produces.Foaming water discharge is exactly to pass through oil pipe or tubing and casing annular space to well
Interior injection foaming water discharge agent generates the foam with certain stability under the agitation of air-flow.The liquid phase that deposition is slipped in pipe becomes
For foam, change the relative density of lower curtate bit stream body in managing, quantity-produced gas phase displacement foam flows out pit shaft, so that well be discharged
Interior hydrops, achievees the purpose that water pumping gas production.
The development of foreign countries' foaming water discharge agent since the eighties of last century sixties, multiselect sulfonate, benzene sulfonate, alkyl
The surfactants such as phenol polyethenoxy ether.Recompounded multielement system is mostly used greatly with foaming water discharge agent to current water pumping gas production, in order to
Enhance the stability of single foam, the auxiliary agents such as alkali, alcohol, polymer, alkanolamide are usually additionally added in formula and form strengthening foam.
US7122509 reports a kind of high temperature foam draining agent prescription, the Research Thinking neutralized using anionic surfactant plus amine,
The heat resistance of raising system is not directed to drainage effect in patent and uses concentration.US20120279715 reports a kind of gas
Gas recovery increases the aerated fluid of oil yield in well, is that a kind of phosphinylidyne-containing amine group quaternary surfactant has both foaming water discharge
And sterilizing function, hydrophobic chain are the hydrophobic patch replaced in naphthalene nucleus, phenyl ring or natural grease, have very strong chlorine-resistant and anticoagulant analysis
The performance of oil also has good corrosion inhibition, the foaming agent of activity concentration 400ppm, foaming water discharge rate in tap water
86.8%, salinity is the analog salt bubbly water foam discharge rate 79.1% of 130000mg/L, however due to containing in molecular structure
The amide group more sensitive to high temperature, thus it is poor to 100 DEG C or more of gas well adaptability.China is from the eighties in last century
Year begins one's study foam drainaging gas cutting process technology, and patent CN102212348A discloses a kind of salt tolerant, methanol tolerance foaming water discharge
Agent, each component content by weight percentage are as follows: Cocoamidopropyl betaine 20~40%, amine oxide 45~65%, alpha-olefin
Sulfonate 5~20%, triethanolamine 5~15%, fluorocarbon surfactant 0.2~2%, methanol 0~5%, can be resistant to salinity
Up to 180,000, foaming agent dosage 5000ppm, but the agent contains fluorocarbon surfactant, and not only cost greatly improves and to environment
It is affected.
The above results show that resisting high temperature, high salt performance difference is the main of restriction high temperature ultra-deep gas well foaming water discharge technology development
Factor.
Summary of the invention
High temperature resistance that the technical problem to be solved by the present invention is to existing foaming water discharge agents under acidic environment is poor, can not
High temperature ultra-deep gas well is solved the problems, such as because of the underproduction even stop-spraying caused by hydrops, provides a kind of ultra-deep gas well using foaming water discharge
The method of agent composition water pumping gas production is applied to high temperature deep well, has very good heat resistance in acid condition, has
Liquid, blistering and foam stability energy are taken by force.
One of to solve above-mentioned technical problem, The technical solution adopted by the invention is as follows: a kind of ultra-deep gas well uses foam
The method of water discharge agent composition water pumping gas production, comprising the following steps:
(1) foaming water discharge agent composition and water are mixed to get foaming water discharge agent composition solution；
(2) foaming water discharge agent composition solution or foaming water discharge agent composition solution and the mixed solution of oil are filled with gas
Tap touching, formed aerated fluid, by the foaming water discharge agent composition solution water or oil water mixture displacement come out；
Wherein, the foaming water discharge agent composition, in terms of mass fraction, including following components:
1) 1 part of polyamines polyether compound；
2) 0.01~100 portion of cosurfactant；
Wherein, the polyamines polyether compound is with general molecular formula shown in formula (1):
In formula (1), R1Selected from C4~C32One of alkyl or substituted hydrocarbon radical, R2、R3、R4It is independently selected from H, C1~C5Alkyl
Carboxylate or substituted hydrocarbon radical carboxylate, C1~C5Hydrocarbyl sulfonate or substituted hydrocarbyl sulfonic acid salt, C1~C5Hydrocarbyl phosphate salt or substitution
Hydrocarbyl phosphate salt and C1~C5At least one of sulfovinic acid ester salt or substituted hydrocarbon radical sulfuric acid, and be not simultaneously H；M is-N
(A)CH2CH2The number of segment, m=1~10；A is substituent group shown in formula (4)；S1, s2, s3 are the adduction that propoxyl group rolls into a ball PO
Number, s1=0~30, s2=0~30, s3=0~30；R1, r2, r3 are the adduction number of ethoxy group EO, r1=0~30, r2=0
~30, r3=0~30, and s1+s2+m*s3 and r1+r2+m*r3 are not zero simultaneously；
The gas is at least one of air, nitrogen, methane or natural gas, can contain or not contain H2S or CO2
Sour gas；The oil is at least one of kerosene, crude oil or condensate.
In above-mentioned technical proposal, the cosurfactant is preferably selected from amphoteric ion or cationic surfactant, yin
At least one of ionic surface active agent；The amphoteric ion or cationic surfactant preferably have to be divided shown in formula (2)
Sub- general formula:
In formula (2), R5For selected from C4~C32One of alkyl or substituted hydrocarbon radical, R6、R7It is independently selected from (CH2)aOH or
(CH2)bCH3One of, R8Selected from (CH2)aOH、(CH2)bCH3、(CH2)cOr (CH2)c(CHOH)d(CH2)eOne of, a=
Any integer in 2~4, any integer in b=0~5, any integer in c=1~4, any integer in d=0~3,
Any integer in e=1~4；N is the adduction number that propoxyl group rolls into a ball PO, n=0~15；P is the adduction number of ethoxy group EO, p=0
~30；X-For selected from OH-, halogen anion, HCO3 -、NO3 -、CH3OSO3 -、CH3COO-、COO-、SO3 -Or OSO3 -One of；
The anionic surfactant preferably has general molecular formula shown in formula (3):
In formula (3), R9With R10The sum of for selected from C4~C32One of alkyl or substituted hydrocarbon radical, M be selected from hydrogen, alkali metal or
Person is by formula NR11(R12)(R13)(R14) shown at least one of group, R11、R12、R13、R14To be independently selected from H, (CH2)aOH or
(CH2)bCH3One of, any integer in a=2~4, b=0~5.
In above-mentioned technical proposal, R1、R5Preferably C8~C24Alkyl or substituted hydrocarbon radical.
In above-mentioned technical proposal, R2、R3、R4Independent is preferably H, CH2COOM1、(CH2)3SO3M1Or CH2(CHOH)
CH2SO3M1One of, and be not simultaneously H.
In above-mentioned technical proposal, R6、R7Preferably CH3、C2H5、(CH2)2OH or C6H5CH2One of.
In above-mentioned technical proposal, the R8Preferably CH3、C2H5、(CH2)2OH or C6H5CH2One of；Or R8X-It is preferred that
For CH2COO-、(CH2)3SO3 -、CH2(CHOH)CH2SO3 -One of.
In above-mentioned technical proposal, R9With R10The sum of preferably C7~C23Alkyl or substituted hydrocarbon radical.
In above-mentioned technical proposal, M and M1Independent is preferably hydrogen, alkali metal or by formula NR11(R12)(R13)(R14) shown in base
At least one of group.
In above-mentioned technical proposal, R11、R12、R13、R14Independent is preferably H, (CH2)aOH or (CH2)bCH3One of.
In above-mentioned technical proposal, preferably a=2~4, b=0~5.
In above-mentioned technical proposal, preferred m=1~5.
In above-mentioned technical proposal, preferred n=0~5；P=0~5.
In above-mentioned technical proposal, preferably s1+s2+m*s3=0~5, r1+r2+m*r3=0~10, and s1+s2+m*s3 and
R1+r2+m*r3 is not zero simultaneously；Further preferred s1+s2+m*s3=1~5, r1+r2+m*r3=1~10.
In above-mentioned technical proposal, it is preferred to steep the mass ratio of polyamines polyether compound and cosurfactant in drain combination object
It is 1: (0.1~10).
In above-mentioned technical proposal, gas preferably is selected from least one of nitrogen, methane or natural gas.
H in above-mentioned technical proposal, in gas2S and CO2Content be preferably 15~35%.
In above-mentioned technical proposal, oil preferably is selected from least one of kerosene or condensate.
The foaming water discharge agent composition key active ingredient that the present invention is suitable for ultra-deep gas well is (1) and (2), this field skill
Art personnel know, for the ease of transporting and storing or scene uses etc. considers, can use various supply forms, such as not
Aqueous solid-state form perhaps aqueous solid-state form perhaps aqueous cream form or aqueous solution form；Aqueous solution shape
Formula includes that the form of concentrate is made into water, is directly made into the solution form of concentration needed for scene drains；Wherein, to water without spy
It is different to require, it can be deionized water, can also be the water containing inorganic mineral, and the water containing inorganic mineral can be originally
Water, gas field water flooding.
In above-mentioned technical proposal, the preparation method of the foaming water discharge agent composition, comprising the following steps:
(1) preparation of polyamines polyether compound
A, amidation process:
By R0COOR ' and H (NHCH2CH2)mNH2, catalyst is with molar ratio 1:(1~2): (0~0.5) mixing, under stirring in
50~200 DEG C of reaction temperature are reacted 3~15 hours, and alcohol or water that reaction generates are evaporated off under normal pressure or reduced pressure, can obtain
To required amide compound R0CO(NHCH2CH2)mNH2；Wherein, R0Selected from C3~C31One of alkyl or substituted hydrocarbon radical, R '
Selected from H, it is selected from C1~C8Alkyl, c=1~10, catalyst be selected from alkali metal hydroxide, alkali metal alcoholates, alkali metal carbonic acid
At least one of salt；
B, reduction reaction:
R0CO(NHCH2CH2)mNH2The method that catalytic hydrogenation can be used in the reduction of middle amide occurs non-equal at high temperature under high pressure
Phase catalytic reaction generates corresponding amine, or uses: the R that step a is synthesized0CO(NHCH2CH2)mNH2With metal hydride H-Y+?
Reduction reaction is carried out in aprotic solvents, obtains R0CH2(NHCH2CH2)cNH2.Wherein, Y+For metallic compound, metal alkyl
Compound, metal amide.
C, poly- etherification reaction:
In the presence of basic catalyst, R that step b is synthesized0CH2(NHCH2CH2)mNH2Successively with aequum epoxy third
Alkane, reacting ethylene oxide obtain long-chain polyamines polyethers intermediate product R0CH2{N[(CHCH3CH2O)s3(CH2CH2O)r3H]
[CH2CH2]}mN[(CHCH3CH2O)s1(CH2CH2O)r1H][CHCH3CH2O)s2(CH2CH2O)r2)H]；
D, carboxylation or sulfonating reaction:
The long-chain polyamines polyethers intermediate product and ionization reagent and alkali that step c is obtained are with molar ratio 1:(1~5): (1
~10) it in a solvent, reacts to generate for 3~20 hours in 50~120 DEG C of reaction temperature and there is polyamines polyethers shown in structural formula (1)
Carboxylate or polyamines polyether sulfonate；The ionization reagent is selected from XR15Y1Or X R '15Y′1At least one of；Described
Alkali is selected from alkali metal hydroxide or alkali metal alcoholates；Y1With Y '1For SO3M1Or COON1, M1And N1For alkali metal, X is chlorine, bromine
Or iodine；
(2) according to required mass fraction, by the polyamines polyether compound of step (1) synthesis, cosurfactant, mixing is equal
It is even, the foaming water discharge agent composition is made.
In above-mentioned technical proposal, R in step a1COOR’、H(NHCH2CH2)mNH2, catalyst mole preferably than 1:(1~
1.3): (0~0.1).
In above-mentioned technical proposal, in step a catalyst be preferably sodium hydroxide, potassium hydroxide, sodium carbonate, in potassium carbonate
It is at least one.
In above-mentioned technical proposal, H in step b-Y+Preferably LiAlH4、LiAlH(OEt)3Or NaBH4At least one of.
In above-mentioned technical proposal, in step b aprotic solvents be preferably ether, tetrahydrofuran, in dioxane extremely
Few one kind.
In above-mentioned technical proposal, long-chain polyamines polyethers intermediate product in step d: ionization reagent: the molar ratio of alkali is preferred
It is 1: (1~2): (1~4).
In above-mentioned technical proposal, solvent described in step d preferably is selected from C3~C8Ketone and C6~C9Aromatic hydrocarbons at least one
Kind, for example, by acetone, butanone, pentanone, from the substance group that benzene, toluene or dimethylbenzene, trimethylbenzene, ethylbenzene and diethylbenzene form
It is at least one.
In above-mentioned technical proposal, the XR15Y1Or X R '15Y′1Example have but be not limited to chloroacetic alkali metal salt, bromine
The alkali metal salt of acetic acid, the alkali metal salt of 3- chlorine-2-hydroxyl propane sulfonic acid, 2- chloroethanes sulfonic acid alkali metal salts etc..
The foaming water discharge agent composition that the present invention is suitable for ultra-deep gas well has good compatibility, can also contain capable
The common other inorganic agents in domain.
In above-mentioned technical proposal, the ultra-deep gas well for example but not limits preferred high temperature acid gas-containing gas reservoir, stratum temperature
Degree is 150~200 DEG C, the total salinity 5000~200000mg/L, H of formation brine2S and CO2Content 0~35%.
What the present invention used contains the long-chain polyamines compound for stablizing chemical bond, can be to avoid under acidic high-temperature high salt conditions
Hydrolysis, keep the stability of molecular structure, utmostly keep foaming water discharge agent foaming water discharge ability.It is of the present invention
The method of the exactly this water pumping gas production suitable for ultra-deep gas well.
The thermal decomposition temperature of polyamines polyether carboxylation prepared by the present invention or polyamines polyether sulfonate at 200 DEG C or more,
It is not hydrolyzed in acidic aqueous solution or very micro hydrolysis, there is good heat resistance；In molecule non-ionic segment and
On the one hand more hydrophilic groups increase salt-resistance, the amount of the combination water and irreducible water that carry foaming agent increases, foam
Liquid carry over enhancing, analysis liquid slow down；Secondly, increasing foam simultaneous with the functional group of yin, yang opposite-sign in foaming water discharge agent
In the adsorbance of gas-liquid interface, the composition of formation is more efficient for agent；In addition, making in molecule containing the hetero atom responded to pH
Obtaining it can be during the acidic high-temperature that low concentration is applied to 150 DEG C or more ultradeep well water pumping gas production with high salt.
It is related to the occasion of foam discharging agent content or concentration in the present invention, refers both to containing component in above-mentioned technical proposal (1)
(2) total content or total concentration.
The method of liquid discharging gas producing of the present invention can also include the methods of gaslift commonly used in the art, machine pumping.
The present invention, which uses the foaming for measuring foaming water discharge agent, foam stabilizing and takes fluidity, can be carried out bubble row's performance evaluation, pass through height
It foaming, foam stabilizing and takes fluidity before and after warm aging and can be carried out comparison, evaluate the high temperature resistance of foaming water discharge agent, specific evaluation method
Are as follows:
(1) bubble row performance
First using the starting foaming height and certain time of Roche foam meter (ROSS-Miles method) measurement foaming water discharge agent
Foaming height afterwards evaluates its foaming capacity and foam stabilizing ability.The gas of certain flow rate is continuously passed through foaming water discharge agent solution
Or foaming water discharge agent solution and oily mixed solution, foam is formed, (water, can also for the measurement liquid that foamover goes out after a certain period of time
Think You Heshui) amount, it calculates and takes liquid rate, evaluate its fluid-carrying capability.
(2) high temperature resistance
Bubble row's performance and Nai Gao after foaming water discharge agent solution high temperature ageing, will be re-started using the acidproof aging equipment of pressure resistance
Warm performance measurement.
Using the method for liquid discharging gas producing of the invention, 0.02~0.12% foaming water discharge agent is in 0~200,000mg/L mine
In change degree salt water, before and after 180 DEG C of high temperature ageings, foam height reaches 175mm, takes liquid rate up to 93.9%, have in acidic environment
There is excellent heat-resistant salt-resistant, blister and take fluidity energy, achieves preferable technical effect.
Below by embodiment, the present invention is further elaborated.
Detailed description of the invention
Fig. 1 is measurement foaming water discharge agent liquid carry over flow diagram.Wherein, 1 is thermostatical water bath, and 2 be measuring cup, and 3 be to follow
Ring water, 4 be foam collection device, and 5 be foaming tube, and 6 be test solution, and 7 be spinner flowmeter, and 8 be gas cylinder.
Specific embodiment
In order to better understand the present invention, the content that the present invention is further explained with reference to embodiments, but it is of the invention
Content is not limited solely to the following examples.
[embodiment 1]
(1) preparation of foam discharging agent FM01
A, 127.6 grams are added in the reaction flask of Xiang Peiyou mechanical stirring, thermometer, dropping funel and atmospheric distillation plant
(0.55 mole) pentaethylene hexamine and 1.4 grams of (0.025 mole) potassium hydroxide solids, 148 grams are slowly instilled under stirring, and (0.5 rubs
You) methyl oleate, reacts 6 hours in 120~160 DEG C of reaction temperature, is collected simultaneously the methanol that reaction generates, can be obtained required
Amide compound C17H33CO(NHCH2CH2)5NH2, yield 93.8%.
B, reflux condensing tube will be housed, dropping funel is added after water removal in the three-necked flask device of thermometer is clean
11.4 grams of lithium aluminium hydride reduction (0.3 mole) and 90 milliliters of dry dioxane, are dispersed with stirring mixing, are added dropwise at -10~5 DEG C and contain 49.6
Gram (0.1 mole) C17H33CO(NHCH2CH2)5NH240wt% dioxane solution, drip slowly be warming up to 35 DEG C or so it is anti-
It answers 3 hours.Reaction solution is carefully poured into ice water, it is post-treated to obtain long-chain polyamines compound C17H33CH2(NHCH2CH2)5NH2, yield 89.0%.
C, 192.8 grams of (0.4 mole) C are added into the pressure reactor equipped with agitating device17H33CH2(NHCH2CH2)5NH2, 4.0 grams of potassium hydroxide, successively with 469.8 grams of (8.1 moles) propylene oxide, 52.8 grams of (1.2 moles) ethylene oxide 140
~160 DEG C of reactions obtain 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2+5s3=20, r1+r2+5r3=3,
R2=R3=R4=H), yield 96.2%.
D, 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2+5s3=20, r1+r2+5r3=3, R2=R3
=R4=H) 177.4 grams (0.1 moles) and 8.0 grams of (0.2 mole) sodium hydroxides, 29.5 grams of (0.15 mole) 3- chlorine-2-hydroxyls
Propanesulfonate and 300 milliliters of toluene/benzene (v/v=1) are mixed in four mouthfuls of burnings equipped with mechanical stirring, thermometer and reflux condensing tube
In bottle, it is heated to 90 DEG C and reacts 7 hours.Solvent is evaporated off, obtains 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2
+ 5s3=20, r1+r2+5r3=3) hydroxypropionate sodium (R2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remaining is
H)。
E, by 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2+5s3=20, r1+r2+5r3=3) hydroxyl
Base propanesulfonate (R2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remaining is H) 50 grams, C16H33OC2H4N+(CH3)3Br-
40 grams, C16H33SO3It 10 grams of K, is uniformly mixed after adding water, the foaming water discharge agent FM01 of 30% content is made.
(2) FM01 is dissolved in deionized water, 100,000mg/L respectively, in 200,000mg/L NaCl water, is configured to
The foam discharging agent mother liquor of 0.3wt%.It is added in Roche foam meter after mother liquor is diluted to a certain concentration, is surveyed using ROSS-Miles method
Determine the starting foaming height and foaming height after five minutes of foam discharging agent FM01, the results are shown in Table 1.
The nitrogen of 4000mL/min is continuously passed through foam discharging agent FM01 aqueous solution, foamover in 15 minutes is measured and goes out
Water, calculating take liquid rate, the results are shown in Table 1.The liquid carry over measurement device of use is as shown in Figure 1.It is acidproof old using pressure resistance
Makeup is set and is tested, and after 180 DEG C of agings for 24 hours, redeterminates starting foaming height, after five minutes foaming height and 15 minutes
The performances such as liquid rate are taken, the results are shown in Table 1.
[embodiment 2]
With [embodiment 1], pH is adjusted to 7 and 4 simulation neutrality and acidity when measuring FM01 performance, with hydrochloric acid by difference
Gaseous environment the results are shown in Table shown in 2.
[embodiment 3]
With [embodiment 1], the difference is that by 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2+5s3
=20, r1+r2+5r3=3) hydroxypropionate sodium (R2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remaining is H) 50
Gram, C16H33OC2H4N+(CH3)3Br-It 50 grams, is uniformly mixed after adding water, the foaming water discharge agent FM02 of 30% content is made, as a result sees
Shown in table 3.
[embodiment 4]
With [embodiment 1], the difference is that by 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2+5s3
=20, r1+r2+5r3=3) hydroxypropionate sodium (R2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remaining is H) 50
Gram, C16H33SO3It 50 grams of Na, is uniformly mixed after adding water, the foaming water discharge agent FM03 of 35% content is made, the results are shown in Table shown in 4.
[embodiment 5]
(1) preparation of foam discharging agent FM04:
A, 67.0 grams are added in the reaction flask of Xiang Peiyou mechanical stirring, thermometer, dropping funel and atmospheric distillation plant
(0.65 mole) diethylenetriamine and 6.9 grams of (0.05 mole) potash solids, 142.0 grams are slowly instilled under stirring, and (0.5 rubs
You) ethyl palmitate, reacts 4 hours in 120~160 DEG C of reaction temperature, is collected simultaneously the ethyl alcohol that reaction generates, institute can be obtained
The amide compound C needed15H31CO(NHCH2CH2)2NH2, yield 94.5%.
B, reflux condensing tube will be housed, dropping funel is added after water removal in the three-necked flask device of thermometer is clean
LiAlH(OEt)351 grams (0.3 moles) and 120 milliliters of anhydrous ethers, are stirred, and are added dropwise at -5~5 DEG C and contain 34.1 gram (0.1
Mole) C15H31CO(NHCH2CH2)2NH250wt% anhydrous ether solution, drip that be slowly warming up to 30 DEG C or so reactions 5 small
When.Reaction solution is carefully poured into ice water, it is post-treated to obtain long-chain polyamines compound C15H31CH2(NHCH2CH2)2NH2, yield
83.4%.
C, 130.8 grams of (0.4 mole) C are added into the pressure reactor equipped with agitating device15H31CH2(NHCH2CH2)2NH2, 5.2 grams of potassium carbonate, successively with 70.8 grams of (1.22 moles) propylene oxide, 35.2 grams of (0.8 mole) ethylene oxide 140~
160 DEG C of reactions obtain 2 (R of long-chain polyamines polyether compound1=C16H33, m=2, s1+s2+2s3=3, r1+r2+2r3=2, R2=
R3=R4=H), yield 97.6%.
D, 2 (R of long-chain polyamines polyether compound1=C16H33, m=2, s1+s2+2s3=3, r1+r2+2r3=2, R2=R3
=R4=H) 58.9 grams (0.1 moles) and 5.7 grams of (0.11 mole) sodium methoxides, 13.4 grams (0.11 mole of third sultone of 1,3- and
100 milliliters of cyclopentanone are mixed in the four-hole boiling flask equipped with mechanical stirring, thermometer and reflux condensing tube, are warming up to back after adding
Stream reaction 5 hours.Solvent is evaporated off, ammonium hydroxide is added, obtains 2 (R of long-chain polyamines polyether compound1=C16H33, m=2, s1+s2+2s3
=3, r1+r2+2r3=2) propane sulfonic acid ammonium (R2、R3、R4One of them is CH2CH2CH2SO3NH4, remaining is H).
E, by 2 (R of long-chain polyamines polyether compound1=C16H33, m=2, s1+s2+2s3=3, r1+r2+2r3=2) third
Ichthyodin 80g, C16H33OC2H4N+(CH3)2CH2COO-It 20 grams, is uniformly mixed after adding water, the foaming water discharge agent of 40% content is made
FM04。
(2) with [embodiment 1], the difference is that aging 72 hours at 150 DEG C, the results are shown in Table shown in 5.
[embodiment 6]
With [embodiment 5], pH is adjusted to 7 and 4 simulation neutrality and acidity when measuring FM04 performance, with hydrochloric acid by difference
Gaseous environment, aging 72 hours, the results are shown in Table shown in 6 at 150 DEG C.
[embodiment 7]
(1) preparation of foam discharging agent FM05:
A, 36.0 grams are added in the reaction flask of Xiang Peiyou mechanical stirring, thermometer, dropping funel and atmospheric distillation plant
(0.6 mole) ethylenediamine and 13.8 grams of (0.1 mole) potash solids, slowly instill 177.0 grams of (0.5 moles) 20 under stirring
Carbomethoxyphenyl reacts 3 hours in 120~160 DEG C of reaction temperature, is collected simultaneously the methanol that reaction generates, can be obtained required
Amide compound C21H43CONHCH2CH2NH2, yield 91.6%.
B, reflux condensing tube will be housed, dropping funel is added after water removal in the three-necked flask device of thermometer is clean
15.2 grams of lithium aluminium hydride reduction (0.4 mole) and 100 milliliters of dry dioxane, are dispersed with stirring mixing, contain in -10~5 DEG C of dropwise additions
38.2 grams of (0.1 mole) C21H43CONHCH2CH2NH240wt% dioxane solution, drip and be slowly warming up to 35 DEG C or so
Reaction 3 hours.Reaction solution is carefully poured into ice water, it is post-treated to obtain long-chain polyamines compound C21H43CH2NHCH2CH2NH2,
Yield 87.9%.
C, 147.2 grams of (0.4 mole) C are added into the pressure reactor equipped with agitating device21H43CH2NHCH2CH2NH2、
5.2 grams of potassium carbonate react to obtain long-chain polyamines polyether compound at 140~160 DEG C with 280.7 grams of (4.84 moles) propylene oxide
3(R1=C22H45, m=1, s1+s2+s3=12, r1+r2+r3=0, R2=R3=R4=H), yield 98.1%.
D, 3 (R of long-chain polyamines polyether compound1=C22H45, m=1, s1+s2+s3=12, r1+r2+r3=0, R2=R3=
R4=H) 106.4 grams (0.1 moles) and 16.8 grams of (0.3 mole) potassium hydroxide, 15.9 grams of (0.12 mole) potassium chloroacetates and 400
Milliliter acetone is mixed in the reaction kettle equipped with mechanical stirring, thermometer and reflux condensing tube, is heated to back flow reaction 10 hours.
Solvent is evaporated off, obtains 3 (R of long-chain polyamines polyether compound1=C22H45, m=1, s1+s2+s3=12, r1+r2+r3=0) second
Sour potassium (R2、R3、R4One of them is CH2COOK, remaining is H).
E, by 3 (R of long-chain polyamines polyether compound1=C22H45, m=1, s1+s2+s3=12, r1+r2+r3=0) acetic acid
Potassium (R2、R3、R4One of them is CH2COOK, remaining is H) 15 grams, C22H45OC2H4N+(CH2CH2OH)2(CH3)CH2COO-90 grams,
Internal olefin sulphonates IOS (C19~23) 30 grams, it is uniformly mixed after adding water, the foaming water discharge agent FM05 of 35% content is made.
(2) with [embodiment 1], the difference is that aging 24 hours at 200 DEG C, the results are shown in Table shown in 7.
[embodiment 8]
With [embodiment 7], pH is adjusted to 7 and 4 simulation neutrality and acidity when measuring FM05 performance, with hydrochloric acid by difference
Gaseous environment, aging 24 hours, the results are shown in Table shown in 8 at 200 DEG C.
[embodiment 9]
(1) preparation of foam discharging agent FM06:
A, 36.0 grams are added in the reaction flask of Xiang Peiyou mechanical stirring, thermometer, dropping funel and atmospheric distillation plant
(0.6 mole) ethylenediamine and 13.8 grams of (0.1 mole) potash solids, slowly instill 158.3 grams of (0.5 mole) rosin under stirring
Sour methyl esters (formula 3) is reacted 8 hours in 120~160 DEG C of reaction temperature, is collected simultaneously the methanol that reaction generates, can be obtained required
Amide compound C19H29CONHCH2CH2NH2, yield 85.6%.
B, reflux condensing tube will be housed, dropping funel is added after water removal in the three-necked flask device of thermometer is clean
13.3 grams of lithium aluminium hydride reduction (0.35 mole) and 100 milliliters of dry dioxane, are dispersed with stirring mixing, contain in -10~5 DEG C of dropwise additions
34.4 grams of (0.1 mole) C19H29CONHCH2CH2NH240wt% dioxane solution, drip and be slowly warming up to 35 DEG C or so
Reaction 5 hours.Reaction solution is carefully poured into ice water, it is post-treated to obtain rosin polyamine compounds C19H29CH2NHCH2CH2NH2,
Yield 73.2%.
C, 132.0 grams of (0.4 mole) C are added into the pressure reactor equipped with agitating device19H29CH2NHCH2CH2NH2、
5.0 grams of potassium hydroxide react to obtain rosin polyamines polyethers chemical combination at 140~160 DEG C with 160.2 grams of (3.64 moles) ethylene oxide
4 (R of object1=C20H31, m=1, s1+s2+s3=0, r1+r2+r3=9, R2=R3=R4=H), yield 91.4%.
D, 4 (R of rosin polyamines polyether compound1=C20H31, m=1, s1+s2+s3=0, r1+r2+r3=9, R2=R3=R4
=H) 72.6 grams (0.1 moles) and 8.0 grams of (0.2 mole) sodium hydroxides, 33.3 grams of (0.2 mole) 2- chloroethene sodium sulfonates and 100
Milliliter toluene is mixed in the reaction kettle equipped with mechanical stirring, thermometer and reflux condensing tube, is heated to back flow reaction 6 hours.
Solvent is evaporated off, obtains 4 (R of long-chain polyamines polyether compound1=C20H31, m=1, s1+s2+s3=0, r1+r2+r3=9) second sulphur
Sour sodium (R2、R3、R4One of them is CH2CH2SO3Na, remaining is H).
E, by 4 (R of long-chain polyamines polyether compound1=C20H31, m=1, s1+s2+s3=0, r1+r2+r3=9) second sulphur
Sour sodium (R2、R3、R4One of them is CH2CH2SO3Na, remaining is H) 90 grams, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5
Gram, a- alkene sulfonate AOS (C14~18) 5 grams, it is uniformly mixed after adding water, the foaming water discharge agent FM06 of 30% content is made.
(2) it with [embodiment 1], the results are shown in Table shown in 9.
[embodiment 10]
With [embodiment 9], pH is adjusted to the high acid gas-containing of 2 simulations when measuring FM06 performance, with hydrochloric acid by difference
Environment the results are shown in Table shown in 10.
[embodiment 11]
With [embodiment 10], the difference is that by 4 (R of long-chain polyamines polyether compound1=C20H31, m=1, s1+s2+s3
=0, r1+r2+r3=9) ethanesulfonic acid sodium (R2、R3、R4One of them is CH2CH2SO3Na, remaining is H) 30 grams,
C16H33C6H4SO390 grams of Na (cetyl benzenesulfonic acid sodium) is uniformly mixed after adding water, the foaming water discharge agent of 30% content is made
FM07 the results are shown in Table shown in 11.
[embodiment 12]
With [embodiment 1], the difference is that the kerosene of certain mass score is added, the results are shown in Table shown in 12 before aging.
[embodiment 13]
With [embodiment 2], the difference is that being passed through in gas acid containing hydrogen sulfide and carbon dioxide when surveying liquid carry over
Gas the results are shown in Table shown in 13.
[comparative example 1]
With [embodiment 1], the difference is that respectively with 1 (R of long-chain polyamines polyether compound1=C18H35, m=5, s1+s2
+ 5s3=20, r1+r2+5r3=3) hydroxypropionate sodium (R2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remaining is
H) 100 grams, C16H33OC2H4N+(CH3)3Br-100 grams, C16H33SO3K100 grams of substitution " 1 (R of long-chain polyamines polyether compound1=
C18H35, m=5, s1+s2+5s3=20, r1+r2+5r3=3) hydroxypropionate sodium (R2、R3、R4One of them is CH2CH
(OH)CH2SO3Na, remaining is H) 50 grams, C16H33OC2H4N+(CH3)3Br-40 grams, C16H33SO310 grams of K " forms foaming water discharge
Agent FM08, FM09 and FM10, simulation water are 100,000mg/LNaCl, be the results are shown in Table shown in 14.
[comparative example 2]
With [embodiment 5], the difference is that respectively with 2 (R of long-chain polyamines polyether compound1=C16H33, m=2, s1+s2
+ 2s3=3, r1+r2+2r3=2) 100 grams of propane sulfonic acid ammonium, C16H33OC2H4N+(CH3)2CH2COO-100 grams of substitution " long-chain polyamines
2 (R of polyether compound1=C16H33, m=2, s1+s2+2s3=3, r1+r2+2r3=2) propane sulfonic acid ammonium 80g, C16H33OC2H4N+
(CH3)2CH2COO-20 grams ", foaming water discharge agent FM11 and FM12 are formed, simulation water is 100,000mg/LNaCl, the results are shown in Table 15
It is shown.
[comparative example 3]
With [embodiment 7], the difference is that with 3 (R of long-chain polyamines polyether compound1=C22H45, m=1, s1+s2+s3
=12, r1+r2+r3=0) potassium acetate (R2、R3、R4One of them is CH2COOK, remaining is H) 135 grams of substitution " long-chain polyamines
3 (R of polyether compound1=C22H45, m=1, s1+s2+s3=12, r1+r2+r3=0) potassium acetate (R2、R3、R4One of them is
CH2COOK, remaining is H) 15 grams, C22H45OC2H4N+(CH2CH2OH)2(CH3)CH2COO-90 grams, internal olefin sulphonates IOS
(C19~23) 30 grams ", foaming water discharge agent FM13 is formed, simulation water is 100,000mg/LNaCl, be the results are shown in Table shown in 15.
[comparative example 4]
With [embodiment 9], the difference is that with 4 (R of long-chain polyamines polyether compound1=C20H31, m=1, s1+s2+s3
=0, r1+r2+r3=9) ethanesulfonic acid sodium (R2、R3、R4One of them is CH2CH2SO3Na, remaining is H) 100 grams of substitution " long-chains
4 (R of polyamines polyether compound1=C20H31, m=1, s1+s2+s3=0, r1+r2+r3=9) ethanesulfonic acid sodium (R2、R3、R4Wherein
One of be CH2CH2SO3Na, remaining is H) 90 grams, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 grams, a- alkene sulfonate
AOS(C14~18) 5 grams ", foaming water discharge agent FM14 is formed, simulation water is 100,000mg/LNaCl, be the results are shown in Table shown in 15.
[comparative example 5]
With [embodiment 1], the difference is that with " C17H33CO(NHCH2CH2)5NH250 grams, C16H33OC2H4N+(CH3)3Br-40 grams, C16H33SO310 grams of K " substitution " long-chain polyamines polyether compound1(R1=C18H35, m=5, s1+s2+5s3=20,
R1+r2+5r3=3 hydroxypropionate sodium (R)2、R3、R4One of them is CH2CH(OH)CH2SO3Na, remaining is H) 50 grams,
C16H33OC2H4N+(CH3)3Br-40 grams, C16H33SO310 grams of K ", forms foaming water discharge agent FM15, and simulation water is 100,000mg/
LNaCl the results are shown in Table shown in 16.
[comparative example 6]
With [comparative example 5], the difference is that pH is adjusted to 7 and 4 simulation neutrality and acid with hydrochloric acid when measurement FM15 performance
Property gaseous environment, the results are shown in Table shown in 17.
[comparative example 7]
With [embodiment 9], the difference is that with " C19H29CONHCH2CH2NH290 grams, C18H37O(C2H4O)2C2H4N+
(CH3)2CH2COO-5 grams, a- alkene sulfonate AOS (C14~18) 5 grams " substitution " 4 (R of long-chain polyamines polyether compound1=C20H31, m
=1, s1+s2+s3=0, r1+r2+r3=9) ethanesulfonic acid sodium (R2、R3、R4One of them is CH2CH2SO3Na, remaining is H) 90
Gram, C18H37O(C2H4O)2C2H4N+(CH3)2CH2COO-5 grams, a- alkene sulfonate AOS (C14~18) 5 grams ", form foaming water discharge agent
FM16, simulation water are 100,000mg/LNaCl, be the results are shown in Table shown in 16.
[comparative example 8]
With [comparative example 7], the difference is that pH is adjusted to 2 simulation height containing sour gas with hydrochloric acid when measurement FM16 performance
Body environment, the results are shown in Table shown in 17.
Table 1
Table 2
Table 3
Table 4
Table 5
Table 6
Table 7
Table 8
Table 9
Table 10
Table 11
Table 12
Table 13
Table 14
Table 15
Table 16
Table 17
Claims (10)
1. a kind of method that ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition, comprising the following steps:
(1) foaming water discharge agent composition and water are mixed to get foaming water discharge agent composition solution；
(2) foaming water discharge agent composition solution or foaming water discharge agent composition solution and the mixed solution of oil are sufficiently connect with gas
Touching, formed aerated fluid, by the foaming water discharge agent composition solution water or oil water mixture displacement come out；
Wherein, the foaming water discharge agent composition, in terms of mass fraction, including following components:
1) 1 part of polyamines polyether compound；
2) 0.01~100 portion of cosurfactant；
Wherein, the polyamines polyether compound is with general molecular formula shown in formula (1):
In formula (1), R1Selected from C4~C32One of alkyl or substituted hydrocarbon radical, R2、R3、R4It is independently selected from H, C1~C5Hydrocarbon carboxylic acids
Salt or substituted hydrocarbon radical carboxylate, C1~C5Hydrocarbyl sulfonate or substituted hydrocarbyl sulfonic acid salt, C1~C5Hydrocarbyl phosphate salt or substituted hydrocarbon radical
Phosphate and C1~C5At least one of sulfovinic acid ester salt or substituted hydrocarbon radical sulfuric acid, and be not simultaneously H；M is-N (A)
CH2CH2The number of segment, m=1~10；A is substituent group shown in formula (4)；S1, s2, s3 are the adduction number that propoxyl group rolls into a ball PO,
S1=0~30, s2=0~30, s3=0~30；R1, r2, r3 be ethoxy group EO adduction number, r1=0~30, r2=0~
30, r3=0~30, and s1+s2+m*s3 and r1+r2+m*r3 are not zero simultaneously；
The gas is at least one of air, nitrogen, methane or natural gas, can contain or not contain H2S or CO2It is acid
Gas；The oil is at least one of kerosene, crude oil or condensate.
2. the method that ultra-deep gas well according to claim 1 uses the water pumping gas production of foaming water discharge agent composition, feature exist
In the cosurfactant in amphoteric ion or cationic surfactant, anionic surfactant at least one
Kind；The amphoteric ion or cationic surfactant have general molecular formula shown in formula (2):
In formula (2), R5For selected from C4~C32One of alkyl or substituted hydrocarbon radical, R6、R7It is independently selected from (CH2)aOH、(CH2)bCH3
Or C6H5CH2One of, R8Selected from (CH2)aOH、(CH2)bCH3、C6H5CH2、(CH2)cOr (CH2)c(CHOH)d(CH2)eIn
One kind, any integer in a=2~4, any integer in b=0~5, any integer in c=1~4, in d=0~3
Any integer, any integer in e=1~4；N is the adduction number that propoxyl group rolls into a ball PO, n=0~15；P is adding for ethoxy group EO
Close number, p=0~30；X-For selected from OH-, halogen anion, HCO3 -、NO3 -、CH3OSO3 -、CH3COO-、COO-、SO3 -Or OSO3 -
One of；
The anionic surfactant has general molecular formula shown in formula (3):
In formula (3), R9With R10The sum of for selected from C3~C31One of alkyl or substituted hydrocarbon radical, M be selected from hydrogen, alkali metal or by
Formula NR11(R12)(R13)(R14) shown at least one of group, R11、R12、R13、R14To be independently selected from H, (CH2)aOH or
(CH2)bCH3One of, any integer in a=2~4, b=0~5.
3. the method that ultra-deep gas well according to claim 2 uses the water pumping gas production of foaming water discharge agent composition, feature exist
In the R1、R5For C8~C24Alkyl or substituted hydrocarbon radical；R9With R10The sum of be C7~C23Alkyl or substituted hydrocarbon radical；R2、R3、R4It is independent
Selected from H, CH2COOM1、(CH2)3SO3M1Or CH2(CHOH)CH2SO3M1One of, and be not simultaneously H, the M1For hydrogen, alkali gold
Belong to or by formula NR11(R12)(R13)(R14) shown at least one of group, R11、R12、R13、R14It is independently selected from H, (CH2)aOH
Or (CH2)bCH3One of, any integer in a=2~4, b=0~5；R6、R7For CH3、C2H5、(CH2)2OH or C6H5CH2
One of；R8For CH3、C2H5、(CH2)2OH or C6H5CH2One of or R8X-For CH2COO-、(CH2)3SO3 -、CH2(CHOH)
CH2SO3 -One of.
4. the method that ultra-deep gas well according to claim 2 uses the water pumping gas production of foaming water discharge agent composition, feature exist
In m=1~5；S1+s2+m*s3=0~5, r1+r2+m*r3=0~10, and s1+s2+m*s3 and r1+r2+m*r3 difference
When be zero；N=0~5, p=0~5.
5. the method that ultra-deep gas well according to claim 1 uses the water pumping gas production of foaming water discharge agent composition, feature exist
In it is described bubble drain combination object in polyamines polyether compound, cosurfactant mass ratio be 1: (0.1~10).
6. the method that any ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition according to claim 1~5,
It is characterized in that the preparation method of the foaming water discharge agent composition, comprising the following steps:
(1) preparation of polyamines polyether compound
A, amidation process:
By R0COOR ' and H (NHCH2CH2)mNH2, catalyst is with molar ratio 1:(1~2): (0~0.5) mixing, in reaction under stirring
50~200 DEG C of temperature are reacted 3~15 hours, and alcohol or water that reaction generates are evaporated off under normal pressure or reduced pressure, institute can be obtained
The amide compound R needed0CO(NHCH2CH2)mNH2；Wherein, R0Selected from C3~C31One of alkyl or substituted hydrocarbon radical, R ' are selected from
H, it is selected from C1~C8Alkyl, c=1~10, catalyst is in alkali metal hydroxide, alkali metal alcoholates, alkali carbonate
At least one；
B, reduction reaction:
R0CO(NHCH2CH2)mNH2The method that the reduction of middle amide uses catalytic hydrogenation, occurs heterogeneous catalysis at high temperature under high pressure
Reaction generates corresponding amine, or uses: the R that step a is synthesized0CO(NHCH2CH2)mNH2With metal hydride H-Y+Non-proton
Reduction reaction is carried out in type solvent, obtains R0CH2(NHCH2CH2)mNH2；Wherein, Y+For metallic compound, metal alkyl chemical combination
Object, metal amide.
C, poly- etherification reaction:
In the presence of basic catalyst, R that step b is synthesized0CH2(NHCH2CH2)cNH2Successively with aequum propylene oxide, ring
Oxidative ethane reacts to obtain long-chain polyamines polyethers intermediate product R0CH2{N[(CHCH3CH2O)s3(CH2CH2O)r3H][CH2CH2]}mN
[(CHCH3CH2O)s1(CH2CH2O)r1H][CHCH3CH2O)s2(CH2CH2O)r2)H]；
D, carboxylation or sulfonating reaction:
The long-chain polyamines polyethers intermediate product and ionization reagent and alkali that step c is obtained are with molar ratio 1:(1~5): (1~10)
In a solvent, it reacts to generate for 3~20 hours in 50~120 DEG C of reaction temperature and there is polyamines polyether carboxylic acid shown in structural formula (1)
Salt or polyamines polyether sulfonate；The ionization reagent is selected from XR15Y1Or XR '15Y′1At least one of；The alkali choosing
From alkali metal hydroxide or alkali metal alcoholates；Y1With Y '1For SO3M1Or COON1, M1And N1For alkali metal, X is chlorine, bromine or iodine；
(2) the polyamines polyether compound of step (1) synthesis, cosurfactant are uniformly mixed according to required mass fraction,
The foaming water discharge agent composition is made.
7. the method that ultra-deep gas well according to claim 6 uses the water pumping gas production of foaming water discharge agent composition, feature exist
The R described in step a0COOR’、H(NHCH2CH2)mNH2, catalyst molar ratio 1:(1~1.3): (0~0.1), catalyst are hydrogen
At least one of sodium oxide molybdena, potassium hydroxide, sodium carbonate, potassium carbonate.
8. the method that ultra-deep gas well according to claim 6 uses the water pumping gas production of foaming water discharge agent composition, feature exist
The H described in step b-Y+For LiAlH4、LiAlH(OEt)3Or NaBH4At least one of, aprotic solvents are ether, tetrahydro
At least one of furans, dioxane；Long-chain polyamines polyethers intermediate product described in step d: ionization reagent: mole of alkali
Than being 1: (1~2): (1~4；The solvent is selected from C3~C8Ketone and C6~C9At least one of aromatic hydrocarbons.
9. the method that ultra-deep gas well according to claim 1 uses the water pumping gas production of foaming water discharge agent composition, feature exist
In the gas be at least one of nitrogen, methane or natural gas, H2S and CO2Content be 15~35%；The oil is coal
At least one of oil or condensate.
10. the method that any ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition according to claim 1~5,
It is characterized in that the ultra-deep gas well formation temperature is 150~200 DEG C, 5000~200000mg/ of total salinity of formation brine
L, H2S and CO2Content 0~35%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710969702.4A CN109679615B (en) | 2017-10-18 | 2017-10-18 | Method for draining water and producing gas by adopting foam water draining agent composition for ultra-deep gas well |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710969702.4A CN109679615B (en) | 2017-10-18 | 2017-10-18 | Method for draining water and producing gas by adopting foam water draining agent composition for ultra-deep gas well |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109679615A true CN109679615A (en) | 2019-04-26 |
| CN109679615B CN109679615B (en) | 2021-07-30 |
Family
ID=66184004
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710969702.4A Active CN109679615B (en) | 2017-10-18 | 2017-10-18 | Method for draining water and producing gas by adopting foam water draining agent composition for ultra-deep gas well |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109679615B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2024002048A1 (en) * | 2022-06-27 | 2024-01-04 | 中国石油化工股份有限公司 | Viscoelastic foam system of acid gas switch, and method and use for improving recovery ratio by using viscoelastic foam system |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030217847A1 (en) * | 1999-07-15 | 2003-11-27 | Reddy B. Raghava | Methods of cementing |
| US20040200616A1 (en) * | 2003-03-25 | 2004-10-14 | Jiten Chatterji | Recyclable foamed fracturing fluids and methods of using the same |
| CN102587865A (en) * | 2012-02-29 | 2012-07-18 | 西南石油大学 | Foam drainage gas recovery method for natural gas horizontal well |
| CN103087698A (en) * | 2013-01-18 | 2013-05-08 | 陕西驭腾实业有限公司 | Solid foamed drainage agent for natural gas well and preparation method of solid foamed drainage agent |
| CN103666431A (en) * | 2012-09-05 | 2014-03-26 | 中国石油化工股份有限公司 | Surfactant composition and preparation method thereof |
| CN104232030A (en) * | 2013-06-17 | 2014-12-24 | 中国石油化工股份有限公司 | Emulsifier for oil base drilling fluid and preparation method thereof |
| CN104830303A (en) * | 2015-05-05 | 2015-08-12 | 中国石油天然气股份有限公司 | Corrosion and scale inhibition foam scrubbing agent and preparation method and application thereof |
| CN104893702A (en) * | 2015-04-28 | 2015-09-09 | 中国石油天然气股份有限公司 | For containing H2Foam discharging agent for water and gas production well drainage and gas production of S gas |
| CN105670591A (en) * | 2016-03-03 | 2016-06-15 | 中国石油天然气股份有限公司 | Anti-freezing foam drainage agent and preparation method and application thereof |
| CN106590604A (en) * | 2015-10-20 | 2017-04-26 | 中国石油化工股份有限公司 | Foaming agent composition for high temperature gas drive and preparation method thereof |
| CN106590568A (en) * | 2015-10-20 | 2017-04-26 | 中国石油化工股份有限公司 | Foam scrubbing agent composition with mineralization resistance for gas recovery by water drainage as well as preparation method and application thereof |
-
2017
- 2017-10-18 CN CN201710969702.4A patent/CN109679615B/en active Active
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030217847A1 (en) * | 1999-07-15 | 2003-11-27 | Reddy B. Raghava | Methods of cementing |
| US20040200616A1 (en) * | 2003-03-25 | 2004-10-14 | Jiten Chatterji | Recyclable foamed fracturing fluids and methods of using the same |
| CN102587865A (en) * | 2012-02-29 | 2012-07-18 | 西南石油大学 | Foam drainage gas recovery method for natural gas horizontal well |
| CN103666431A (en) * | 2012-09-05 | 2014-03-26 | 中国石油化工股份有限公司 | Surfactant composition and preparation method thereof |
| CN103087698A (en) * | 2013-01-18 | 2013-05-08 | 陕西驭腾实业有限公司 | Solid foamed drainage agent for natural gas well and preparation method of solid foamed drainage agent |
| CN104232030A (en) * | 2013-06-17 | 2014-12-24 | 中国石油化工股份有限公司 | Emulsifier for oil base drilling fluid and preparation method thereof |
| CN104893702A (en) * | 2015-04-28 | 2015-09-09 | 中国石油天然气股份有限公司 | For containing H2Foam discharging agent for water and gas production well drainage and gas production of S gas |
| CN104830303A (en) * | 2015-05-05 | 2015-08-12 | 中国石油天然气股份有限公司 | Corrosion and scale inhibition foam scrubbing agent and preparation method and application thereof |
| CN106590604A (en) * | 2015-10-20 | 2017-04-26 | 中国石油化工股份有限公司 | Foaming agent composition for high temperature gas drive and preparation method thereof |
| CN106590568A (en) * | 2015-10-20 | 2017-04-26 | 中国石油化工股份有限公司 | Foam scrubbing agent composition with mineralization resistance for gas recovery by water drainage as well as preparation method and application thereof |
| CN105670591A (en) * | 2016-03-03 | 2016-06-15 | 中国石油天然气股份有限公司 | Anti-freezing foam drainage agent and preparation method and application thereof |
Non-Patent Citations (7)
| Title |
|---|
| ALHASAN FUSENI: "Evaluation of foaming agents for EOR application in carbonated reserviors", 《THE SPE EOR CONFERENCE AT OIL AND GAS WEST ASIA》 * |
| 姜兆华等: "《应用表面化学》", 28 February 2009, 哈尔滨工业大学出版社 * |
| 曾庆恒: "《采气工程》", 31 August 1999, 石油工业出版社 * |
| 汪多仁: "《精细化工中间体》", 31 January 2008, 海洋出版社 * |
| 董国君等: "《表面活性剂化学》", 31 August 2009, 北京理工大学出版社 * |
| 邢存章等: "《山东省教育厅"九五"立项教材 有机化学 下册》", 31 January 2001, 山东大学出版社 * |
| 龚浩研: "泡沫排水采气在气田开发中的研究及应用", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2024002048A1 (en) * | 2022-06-27 | 2024-01-04 | 中国石油化工股份有限公司 | Viscoelastic foam system of acid gas switch, and method and use for improving recovery ratio by using viscoelastic foam system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109679615B (en) | 2021-07-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104232044B (en) | Surface activator composition, preparation method and application for tertiary oil recovery | |
| CN104232045B (en) | Composite surface active agent composition and preparation method and application thereof | |
| CN103773351B (en) | High salinity reservoir gas drive foam compositions and preparation method and purposes | |
| CN103740354B (en) | A surfactant composition used for tertiary oil recovery and a preparation method thereof | |
| CN106590577A (en) | Foam composition and preparation method of the same | |
| CN104277814B (en) | Surfactant oil displacement composition, preparation method and application | |
| CN103003385A (en) | Guerbet alcohol alkoxylate surfactants and their use in enhanced oil recovery applications | |
| CN101619209B (en) | New application and composition of amide sodium sulfonate as oil field additive | |
| CN102516064A (en) | Preparation method of nonionic-anionic compound type surfactant and application thereof | |
| CN106590606A (en) | Temperature and salt resisting low-tension foam and application thereof in foam plugging | |
| CN103740357A (en) | Low-tension foaming agent composition and preparation method thereof | |
| CN105368430A (en) | Oil-displacing agent, preparing method of oil-displacing agent and intensified oil production method | |
| CN109681175A (en) | Using the method for the solid foam water discharge agent liquid discharging gas producing of pH value response | |
| CN106590567A (en) | Low tension foaming agent for high-salinity strata, and preparation method and applications thereof | |
| CN109679607A (en) | Using the method for resisting high temperature, high salt foaming water discharge agent water pumping gas production | |
| CN109679615A (en) | The method that ultra-deep gas well uses the water pumping gas production of foaming water discharge agent composition | |
| CN109679631A (en) | Ultra-deep gas well foaming water discharge agent composition and preparation method and application | |
| CN109401743B (en) | Foam scrubbing agent composition for salt-resistant acid-resistant water drainage and gas production and preparation method and application thereof | |
| CN109679637A (en) | The method that ultra-deep gas well uses the composition water pumping gas production of solid foam water discharge agent | |
| CN109679608A (en) | High temperature resistant acid resistant form foaming water discharge agent and preparation method and application | |
| CN109679609A (en) | Foaming water discharge agent composition and preparation method and application suitable for ultra-deep gas well | |
| CN104232047B (en) | Three using surface activator composition, preparation method and application | |
| CN109679616A (en) | The foaming water discharge agent and preparation method and application of pH value response | |
| CN109679617A (en) | Solid foam water discharge agent composition and preparation method and application suitable for ultra-deep gas well | |
| CN109679610A (en) | The solid foam water discharge agent and preparation method and application of pH value response |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |