CN106279706A - A kind of preparation method of polyether grafting chitosan derivatives crude oil desalting demulsifier - Google Patents
A kind of preparation method of polyether grafting chitosan derivatives crude oil desalting demulsifier Download PDFInfo
- Publication number
- CN106279706A CN106279706A CN201610644993.5A CN201610644993A CN106279706A CN 106279706 A CN106279706 A CN 106279706A CN 201610644993 A CN201610644993 A CN 201610644993A CN 106279706 A CN106279706 A CN 106279706A
- Authority
- CN
- China
- Prior art keywords
- chitosan
- preparation
- crude oil
- demulsifier
- monomethyl ether
- 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
- 229920001661 Chitosan Polymers 0.000 title claims abstract description 99
- 239000010779 crude oil Substances 0.000 title claims abstract description 54
- 238000002360 preparation method Methods 0.000 title claims abstract description 40
- 239000004721 Polyphenylene oxide Substances 0.000 title claims abstract description 32
- 229920000570 polyether Polymers 0.000 title claims abstract description 32
- 238000011033 desalting Methods 0.000 title claims abstract description 13
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 claims abstract description 45
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 41
- 125000004181 carboxyalkyl group Chemical group 0.000 claims abstract description 33
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 claims abstract 3
- 238000006243 chemical reaction Methods 0.000 claims description 64
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 39
- -1 dimethyl alkylamine Chemical class 0.000 claims description 30
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 29
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 26
- 238000003756 stirring Methods 0.000 claims description 26
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 24
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 24
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical group CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 claims description 18
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 18
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 16
- 239000002904 solvent Substances 0.000 claims description 14
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 12
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 12
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-dimethylformamide Substances CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 9
- 239000003153 chemical reaction reagent Substances 0.000 claims description 7
- 239000012153 distilled water Substances 0.000 claims description 7
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 6
- 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 claims description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical class N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims description 6
- 239000003638 chemical reducing agent Substances 0.000 claims description 6
- 239000011734 sodium Substances 0.000 claims description 6
- 229910052708 sodium Inorganic materials 0.000 claims description 6
- 239000012279 sodium borohydride Substances 0.000 claims description 6
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 238000007037 hydroformylation reaction Methods 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 4
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 4
- 150000004676 glycans Chemical class 0.000 claims description 4
- 229920001282 polysaccharide Polymers 0.000 claims description 4
- 239000005017 polysaccharide Substances 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 3
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 3
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- 239000011261 inert gas Substances 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 2
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- BEOOHQFXGBMRKU-UHFFFAOYSA-N sodium cyanoborohydride Chemical compound [Na+].[B-]C#N BEOOHQFXGBMRKU-UHFFFAOYSA-N 0.000 claims description 2
- 239000000725 suspension Substances 0.000 claims description 2
- 238000001291 vacuum drying Methods 0.000 claims description 2
- 229920000151 polyglycol Polymers 0.000 claims 6
- 239000010695 polyglycol Substances 0.000 claims 6
- BQFCCCIRTOLPEF-UHFFFAOYSA-N chembl1976978 Chemical compound CC1=CC=CC=C1N=NC1=C(O)C=CC2=CC=CC=C12 BQFCCCIRTOLPEF-UHFFFAOYSA-N 0.000 claims 4
- 239000000376 reactant Substances 0.000 claims 4
- 239000003513 alkali Substances 0.000 claims 3
- 238000004108 freeze drying Methods 0.000 claims 3
- 238000010792 warming Methods 0.000 claims 3
- LRWZZZWJMFNZIK-UHFFFAOYSA-N 2-chloro-3-methyloxirane Chemical compound CC1OC1Cl LRWZZZWJMFNZIK-UHFFFAOYSA-N 0.000 claims 2
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 claims 2
- 125000004965 chloroalkyl group Chemical group 0.000 claims 2
- 238000005660 chlorination reaction Methods 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 229910052756 noble gas Inorganic materials 0.000 claims 1
- 238000001556 precipitation Methods 0.000 claims 1
- 230000008961 swelling Effects 0.000 claims 1
- 239000002202 Polyethylene glycol Substances 0.000 abstract description 38
- 230000018044 dehydration Effects 0.000 abstract description 17
- 238000006297 dehydration reaction Methods 0.000 abstract description 17
- 238000010612 desalination reaction Methods 0.000 abstract description 15
- 230000000694 effects Effects 0.000 abstract description 12
- 239000000839 emulsion Substances 0.000 abstract description 9
- 230000004048 modification Effects 0.000 abstract description 9
- 238000012986 modification Methods 0.000 abstract description 9
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 abstract description 8
- 235000019270 ammonium chloride Nutrition 0.000 abstract description 7
- 150000003839 salts Chemical class 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 6
- 150000001768 cations Chemical class 0.000 abstract description 4
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 4
- 150000003242 quaternary ammonium salts Chemical group 0.000 abstract description 4
- 239000002994 raw material Substances 0.000 abstract description 4
- 150000002500 ions Chemical class 0.000 abstract description 3
- 125000005609 naphthenate group Chemical group 0.000 abstract description 3
- 231100000252 nontoxic Toxicity 0.000 abstract description 3
- 230000003000 nontoxic effect Effects 0.000 abstract description 3
- 239000002245 particle Substances 0.000 abstract description 2
- 229920002521 macromolecule Polymers 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 47
- 238000000034 method Methods 0.000 description 19
- 230000000052 comparative effect Effects 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- 239000003921 oil Substances 0.000 description 10
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 10
- 239000012265 solid product Substances 0.000 description 10
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 description 8
- 239000011541 reaction mixture Substances 0.000 description 8
- 230000022244 formylation Effects 0.000 description 7
- 238000006170 formylation reaction Methods 0.000 description 7
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 6
- 239000012295 chemical reaction liquid Substances 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 5
- 239000003999 initiator Substances 0.000 description 5
- 229910000027 potassium carbonate Inorganic materials 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000000706 filtrate Substances 0.000 description 4
- 239000012299 nitrogen atmosphere Substances 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 238000010291 electrical method Methods 0.000 description 3
- DYBLTIDRXDSCKH-UHFFFAOYSA-M hexadecyl-dimethyl-(oxiran-2-ylmethyl)azanium;chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCC[N+](C)(C)CC1CO1 DYBLTIDRXDSCKH-UHFFFAOYSA-M 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 229920005615 natural polymer Polymers 0.000 description 3
- 239000011241 protective layer Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 229920002101 Chitin Polymers 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000012043 crude product Substances 0.000 description 2
- GLIVMJADAWRCMK-UHFFFAOYSA-M dimethyl-(oxiran-2-ylmethyl)-tetradecylazanium;chloride Chemical compound [Cl-].CCCCCCCCCCCCCC[N+](C)(C)CC1CO1 GLIVMJADAWRCMK-UHFFFAOYSA-M 0.000 description 2
- ALNUPAIRBMNLLB-UHFFFAOYSA-M dodecyl-dimethyl-(oxiran-2-ylmethyl)azanium;chloride Chemical compound [Cl-].CCCCCCCCCCCC[N+](C)(C)CC1CO1 ALNUPAIRBMNLLB-UHFFFAOYSA-M 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 229920000768 polyamine Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- LCPUCXXYIYXLJY-UHFFFAOYSA-N 1,1,2,4,4,4-hexafluorobutyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC(F)(F)C(F)CC(F)(F)F LCPUCXXYIYXLJY-UHFFFAOYSA-N 0.000 description 1
- OSNIIMCBVLBNGS-UHFFFAOYSA-N 1-(1,3-benzodioxol-5-yl)-2-(dimethylamino)propan-1-one Chemical compound CN(C)C(C)C(=O)C1=CC=C2OCOC2=C1 OSNIIMCBVLBNGS-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- DZMQPTWLXKIMCW-UHFFFAOYSA-M CCCCCCCCCCCCCCCCCCCCCC[N+](C)(C)CC1OC1.[Cl-] Chemical compound CCCCCCCCCCCCCCCCCCCCCC[N+](C)(C)CC1OC1.[Cl-] DZMQPTWLXKIMCW-UHFFFAOYSA-M 0.000 description 1
- 239000004970 Chain extender Substances 0.000 description 1
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- RVGRUAULSDPKGF-UHFFFAOYSA-N Poloxamer Chemical compound C1CO1.CC1CO1 RVGRUAULSDPKGF-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 125000005210 alkyl ammonium group Chemical group 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 230000021523 carboxylation Effects 0.000 description 1
- 238000006473 carboxylation reaction Methods 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 230000006196 deacetylation Effects 0.000 description 1
- 238000003381 deacetylation reaction Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000006266 etherification reaction Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 125000001165 hydrophobic group Chemical group 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 238000005956 quaternization reaction Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- FDRCDNZGSXJAFP-UHFFFAOYSA-M sodium chloroacetate Chemical compound [Na+].[O-]C(=O)CCl FDRCDNZGSXJAFP-UHFFFAOYSA-M 0.000 description 1
- GNBYZUQCDMNXML-UHFFFAOYSA-M sodium;2-chlorobutanoate Chemical compound [Na+].CCC(Cl)C([O-])=O GNBYZUQCDMNXML-UHFFFAOYSA-M 0.000 description 1
- RPOHBMAQTOJHKM-UHFFFAOYSA-M sodium;2-chloropropanoate Chemical compound [Na+].CC(Cl)C([O-])=O RPOHBMAQTOJHKM-UHFFFAOYSA-M 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000007762 w/o emulsion Substances 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G81/00—Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0024—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
- C08B37/0027—2-Acetamido-2-deoxy-beta-glucans; Derivatives thereof
- C08B37/003—Chitin, i.e. 2-acetamido-2-deoxy-(beta-1,4)-D-glucan or N-acetyl-beta-1,4-D-glucosamine; Chitosan, i.e. deacetylated product of chitin or (beta-1,4)-D-glucosamine; Derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
- C08G65/48—Polymers modified by chemical after-treatment
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/04—Dewatering or demulsification of hydrocarbon oils with chemical means
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Molecular Biology (AREA)
- Cosmetics (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
本发明涉及一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备方法。具体步骤如下:(1)将聚乙二醇单甲醚进行醛基化改性;(2)制备缩水甘油基二甲基烷基氯化铵;(3)制备季铵化羧烷基壳聚糖;(4)将醛基化改性聚乙二醇单甲醚与季铵化羧烷基壳聚糖反应,得到聚醚接枝壳聚糖衍生物原油脱盐破乳剂。本发明以壳聚糖类天然高分子化合物为原料,具有来源广泛、天然、无毒、可持续、产物生物兼容性好、可降解等诸多优点。制备得到的破乳剂不仅破乳脱水效果好,同时由于破乳剂分子上含有大量的羧烷基基团和季铵盐基团,对金属阳离子、环烷酸根等带负电的离子及表面呈负电性的颗粒有很强的结合能力,因此在破乳的同时兼具脱除油溶性盐的能力。The invention relates to a preparation method of a polyether grafted chitosan derivative crude oil desalting demulsifier. The specific steps are as follows: (1) carry out aldehyde modification of polyethylene glycol monomethyl ether; (2) prepare glycidyl dimethyl alkyl ammonium chloride; (3) prepare quaternized carboxyalkyl chitosan sugar; (4) reacting aldehydized modified polyethylene glycol monomethyl ether with quaternized carboxyalkyl chitosan to obtain polyether grafted chitosan derivative crude oil desalination demulsifier. The invention uses chitosan natural macromolecular compounds as raw materials, and has many advantages such as wide source, natural, non-toxic, sustainable, good biocompatibility and degradability of products. The prepared demulsifier not only has a good demulsification and dehydration effect, but also has a negative charge on the negatively charged ions such as metal cations and naphthenate groups and the surface due to the large number of carboxyalkyl groups and quaternary ammonium salt groups on the demulsifier molecules. The particles have a strong binding ability, so it has the ability to remove oil-soluble salts while breaking the emulsion.
Description
技术领域technical field
本发明涉及一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备方法,属于石油化工领域。The invention relates to a preparation method of a polyether grafted chitosan derivative crude oil desalination demulsifier, belonging to the field of petrochemical industry.
背景技术Background technique
随着工业的迅速发展,石油的需求量越来越大,提高石油采收率具有非常重要的意义。由于化学驱的使用量不断增大,加之原油的重质化和高酸值化日益严重,原油中的金属离子含量逐渐上升。原油中的盐主要是无机盐,大都溶于其所含的水中,水与油形成了稳定的油包水(W/O)型乳状液。原油脱盐的关键在于脱水,而脱水的关键在于破乳。原油中的天然乳化液吸附在油水界面,形成具有一定强度的粘弹性膜,给乳滴聚结造成了动力学障碍,使原油乳状液具有了稳定性。破乳的原则是破坏乳状液稳定的因素,国内外对原油破乳研究较多成功开发了许多破乳方法。油田最常用的是加入破乳剂,破乳剂是当今油田和炼厂必不可少的化学试剂之一。随着石油工业的发展,破乳剂的需求量日益增加,对其性能要求也更为苛刻。如果开发出一种新型高效的深度脱盐破乳剂,在破乳的同时能够脱除油溶性盐,将对我国原油加工有十分重要的意义。With the rapid development of industry, the demand for oil is increasing, and it is of great significance to enhance oil recovery. As the use of chemical flooding continues to increase, coupled with the increasingly heavy and high acid value of crude oil, the content of metal ions in crude oil is gradually increasing. The salts in crude oil are mainly inorganic salts, most of which are soluble in the water contained in them, and water and oil form a stable water-in-oil (W/O) emulsion. The key to desalting crude oil is dehydration, and the key to dehydration is demulsification. The natural emulsion in crude oil is adsorbed at the oil-water interface to form a viscoelastic film with a certain strength, which creates a dynamic obstacle for the coalescence of emulsion droplets and makes the crude oil emulsion stable. The principle of demulsification is the factor that destroys the stability of the emulsion. There are many researches on demulsification of crude oil at home and abroad, and many demulsification methods have been successfully developed. The most commonly used in oil field is to add demulsifier, demulsifier is one of the essential chemical reagents in today's oil field and refinery. With the development of the petroleum industry, the demand for demulsifiers is increasing, and the performance requirements are more stringent. If a new type of high-efficiency deep desalination demulsifier is developed, which can remove oil-soluble salts while breaking the demulsification, it will be of great significance to my country's crude oil processing.
原油破乳的方法主要有化学法、电法、离心分离法、超声波法、生物法等。其中化学法和电法最常用,但电法对设备及工艺条件要求较高,实施比较复杂,前期投入和后期运行费用都比较高;化学法是一种经济合理的方法。Crude oil demulsification methods mainly include chemical method, electrical method, centrifugal separation method, ultrasonic method, biological method and so on. Among them, the chemical method and the electrical method are the most commonly used, but the electrical method has higher requirements on equipment and process conditions, the implementation is more complicated, and the initial investment and later operation costs are relatively high; the chemical method is an economical and reasonable method.
破乳剂的破乳过程一般分为3个阶段:(1)破乳剂加入原油乳状液后,让它分散在整个油相中,并能进入被乳化的水珠内;(2)破乳剂渗入到乳化水珠的保护层,并使保护层脆弱变皱破坏,保护层破坏后,被乳化的水珠互相接近并接触;(3)水珠聚结,被乳化的水珠从连续向分离出来。The demulsification process of the demulsifier is generally divided into three stages: (1) After the demulsifier is added to the crude oil emulsion, it is dispersed in the entire oil phase and can enter the emulsified water droplets; (2) The demulsifier penetrates into the Emulsify the protective layer of water droplets, and make the protective layer fragile, wrinkled and damaged. After the protective layer is destroyed, the emulsified water droplets approach and contact each other; (3) the water droplets coalesce, and the emulsified water droplets are separated from the continuous direction.
从1914年报道的Barnickel用0.1%的FeS04溶液在35℃~60℃使乳化原油破乳起,先后开发出三代破乳剂。20世纪20年代至30年代为解决水包油型原油乳状液破乳,出现了第一代低分子离子型破乳剂,如脂肪酸盐、环烷酸盐等阴离子型破乳剂,季铵盐类阳离子型破乳剂。此类型破乳剂优点是价格低廉,缺点是用量大、效果差、易受电解质的影响等。20世纪40年代至50年代,环氧乙烷生产的工业化促使了环氧乙烷环氧丙烷嵌段共聚物的出现。由此发展了第二代油包水乳化原油的破乳剂,主要是低分子非离子型表面活性剂。自20世纪60年代以后,人们开发出第三代以高相对分子质量聚醚为主的破乳剂。国外对原油破乳剂进行了大量的研究,提出了大量的专利。最早作为破乳剂的非离子表面活性剂是以烷基酚、脂肪醇作为憎水基团,接枝共聚一定数量的环氧乙烷制备的。随着三次采油技术的大规模现场实验,新型原油破乳剂不断涌现。进入80年代后,单纯环氧乙烷环氧丙烷嵌段聚醚破乳剂开始被聚胺类、聚合物型、两性离子型破乳剂所取代,最低用量降到100mg/L以下。但这些破乳剂的缺点是专一性强,适应性差。因此人们又通过改性或复配研制复合破乳剂以及超高分子量高效破乳剂,从而把破乳剂的应用研究推向了一个新的台阶。Since Barnickel reported in 1914 to use 0.1% FeSO 4 solution to demulsify the emulsified crude oil at 35°C to 60°C, three generations of demulsifiers have been developed successively. From the 1920s to the 1930s, in order to solve the demulsification of oil-in-water crude oil emulsions, the first generation of low-molecular-weight ionic demulsifiers appeared, such as fatty acid salts, naphthenates and other anionic demulsifiers, quaternary ammonium salts, etc. Cationic demulsifier. The advantage of this type of demulsifier is low price, and the disadvantages are large dosage, poor effect, and easy to be affected by electrolytes. The industrialization of ethylene oxide production in the 1940s and 1950s led to the emergence of ethylene oxide and propylene oxide block copolymers. Thus, the second generation of demulsifiers for water-in-oil emulsified crude oil has been developed, mainly low-molecular non-ionic surfactants. Since the 1960s, people have developed the third generation of demulsifiers based on high molecular weight polyether. A lot of research has been done on crude oil demulsifier abroad, and a lot of patents have been proposed. The earliest nonionic surfactants used as demulsifiers were prepared by grafting and copolymerizing a certain amount of ethylene oxide with alkylphenols and fatty alcohols as hydrophobic groups. With the large-scale field experiments of tertiary oil recovery technology, new crude oil demulsifiers are constantly emerging. After entering the 1980s, pure ethylene oxide propylene oxide block polyether demulsifiers began to be replaced by polyamines, polymers, and zwitterionic demulsifiers, and the minimum dosage dropped below 100mg/L. However, the disadvantages of these demulsifiers are strong specificity and poor adaptability. Therefore, people have developed composite demulsifiers and ultra-high molecular weight high-efficiency demulsifiers through modification or compounding, thus pushing the application research of demulsifiers to a new level.
为解决上述问题,近年来出现多起始剂制备原油破乳剂的方法。中国专利CN200510130345介绍了一种聚醚型原油破乳剂。以多乙烯多胺或壬基酚醛树脂为起始剂,与环氧乙烷、环氧丙烷反应得到聚醚,再将聚醚与扩链剂、吡啶混合反应得到。该发明有制备工艺简单,用量少,破乳脱水效果好,成本低等优点,但该破乳剂不能达到低温破乳以节省热能的效果。中国专利CN 201410710742介绍了一种低温原油破乳剂。以甲基丙烯酸缩水甘油酯、甲基丙烯酸六氟丁酯为起始剂与丙酮、丙烯酸共聚得到。规避了现有产品破乳所需温度高,破乳时间长,脱水水质差的弊端。能在低温下破乳,降低吨油耗气量、节省能源、提高经济效益和设备处理效率。但该破乳剂专一性强,稳定性较差,不能适合多种不同类型的原油破乳。中国专利CN 201310289037.6介绍了一种多糖改性的原油破乳剂。以多糖为起始剂,并对其进行季铵化改性,聚醚接枝改性,该破乳剂具有来源广泛、天然、无毒、可持续、使用安全性好等诸多优点。该破乳剂不仅破乳脱水效果好,破乳剂分子中含有的大量羟基等基团对金属离子有一定的鳌合能力,但结合能力不强,不能在脱水的同时脱出不同种类和大量的金属阳离子,还需进行改善。因此,需要开发一种低温破乳,快速破乳,扩大破乳剂对原油适用范围以及兼具良好脱水脱盐效果的破乳剂。In order to solve the above problems, a method for preparing crude oil demulsifiers with multiple initiators has emerged in recent years. Chinese patent CN200510130345 introduces a polyether type crude oil demulsifier. Polyethylene polyamine or nonylphenolic resin is used as the initiator to react with ethylene oxide and propylene oxide to obtain polyether, and then the polyether is mixed with chain extender and pyridine to obtain it. The invention has the advantages of simple preparation process, less dosage, good demulsification and dehydration effect, low cost, etc., but the demulsifier cannot achieve the effect of low temperature demulsification to save heat energy. Chinese patent CN 201410710742 introduces a low-temperature crude oil demulsifier. It is obtained by copolymerizing glycidyl methacrylate and hexafluorobutyl methacrylate with acetone and acrylic acid as initiators. The disadvantages of high temperature required for demulsification, long demulsification time and poor dehydration water quality of existing products are avoided. It can break emulsion at low temperature, reduce gas consumption per ton of oil, save energy, improve economic benefits and equipment processing efficiency. However, this demulsifier has strong specificity and poor stability, and cannot be suitable for demulsification of many different types of crude oil. Chinese patent CN 201310289037.6 introduces a polysaccharide modified crude oil demulsifier. The polysaccharide is used as the starting agent, and it is modified by quaternization and polyether grafting. The demulsifier has many advantages such as wide source, natural, non-toxic, sustainable, and good use safety. The demulsifier not only has a good effect of demulsification and dehydration, but also a large number of hydroxyl groups and other groups contained in the demulsifier molecule have a certain ability to chelate metal ions, but the binding ability is not strong, and it cannot remove different types and a large number of metal cations during dehydration. , still need to be improved. Therefore, it is necessary to develop a low-temperature demulsification, rapid demulsification, expand the application range of the demulsifier to crude oil, and have a good dehydration and desalination effect.
甲壳素来源广泛,含量仅次于纤维素,为世界第二大类的有机化合物。壳聚糖是甲壳素脱乙酰基的产物,与黄原胶和瓜尔豆胶相比,分子链上含有反应活性更大的氨基,更易接枝改性。壳聚糖类天然高分子具有极好的生物相容性和环境友好性,分子量大、活泼氢多、具有分支结构和独特的流变学性能。其衍生物具有较强的絮凝能力,在油水界面所占据的面积大,具有较好的耐温性、较高的界面活性,是破乳剂起始剂的极佳的候选对象。壳聚糖分子链上引入羧烷基和季铵盐基团对原油中金属阳离子、环烷酸根等带负电的离子有很强的结合能力。同时通过控制各取代基的位置和取代度,以及聚醚侧链,羧烷基基团和季铵盐基团上链段的长度,可得到一系列合适于不同性质原油的高效破乳剂,且可以在破乳的同时脱去油溶性盐。Chitin has a wide range of sources, and its content is second only to cellulose, which is the second largest type of organic compound in the world. Chitosan is the product of deacetylation of chitin. Compared with xanthan gum and guar gum, the molecular chain contains more reactive amino groups and is easier to graft and modify. Chitosan natural polymer has excellent biocompatibility and environmental friendliness, large molecular weight, many active hydrogen, branched structure and unique rheological properties. Its derivatives have strong flocculation ability, occupy a large area at the oil-water interface, have good temperature resistance and high interfacial activity, and are excellent candidates for demulsifier initiators. The introduction of carboxyalkyl groups and quaternary ammonium salt groups into the molecular chain of chitosan has a strong binding ability to negatively charged ions such as metal cations and naphthenate groups in crude oil. At the same time, by controlling the position and degree of substitution of each substituent, as well as the length of the polyether side chain, carboxyalkyl group and quaternary ammonium salt group, a series of high-efficiency demulsifiers suitable for crude oil with different properties can be obtained, and Oil-soluble salts can be removed while breaking the emulsification.
发明内容Contents of the invention
本发明的目的是针对上述现有技术中存在的问题而提出一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备方法,得到一系列合适于不同性质原油,且可以在破乳的同时脱去油溶性盐的高效破乳剂。The purpose of the present invention is to propose a kind of preparation method of polyether grafted chitosan derivative crude oil desalination demulsifier for the problems existing in the above-mentioned prior art, obtain a series of crude oils suitable for different properties, and can be used in demulsification Efficient demulsifier for removing oil-soluble salts at the same time.
为实现上述目的,本发明提供的技术方案是:To achieve the above object, the technical solution provided by the invention is:
一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备方法,其特征在于,包括以下步骤:A preparation method of polyether grafted chitosan derivative crude oil desalination demulsifier, is characterized in that, comprises the following steps:
1)将聚乙二醇单甲醚端羟基进行醛化得醛化改性聚乙二醇单甲醚;1) carrying out hydroformylation of polyethylene glycol monomethyl ether terminal hydroxyl groups to obtain hydroformylated modified polyethylene glycol monomethyl ether;
2)缩水甘油基二甲基烷基氯化铵的制备:向N,N‐二甲基烷基胺中滴加环氧氯丙烷,升温至25℃~40℃,恒温反应6~30h,将反应产物分离纯化,得到缩水甘油基二甲基烷基氯化铵;其中所述N,N‐二甲基烷基胺中烷基的碳链长度为C6‐C34;2) Preparation of glycidyl dimethyl alkyl ammonium chloride: Add epichlorohydrin dropwise to N,N-dimethyl alkyl amine, raise the temperature to 25°C-40°C, and react at constant temperature for 6-30h. The reaction product is separated and purified to obtain glycidyl dimethyl alkyl ammonium chloride; wherein the carbon chain length of the alkyl group in the N,N-dimethyl alkylamine is C 6 -C 34 ;
3)季铵化羧烷基壳聚糖的制备:将羧烷基壳聚糖采用溶剂A溶解,采用碱液调节溶液pH值,再将步骤2)所得的缩水甘油基二甲基烷基氯化铵溶解于溶剂A中,滴加至反应体系,升温至60~80℃,反应8~24h后,将反应液透析,冷冻干燥,得到固体产物季铵化羧烷基壳聚糖;3) Preparation of quaternized carboxyalkyl chitosan: dissolving carboxyalkyl chitosan in solvent A, adjusting the pH value of the solution with lye, and then dissolving the glycidyl dimethyl alkyl chloride obtained in step 2) Dissolve ammonium chloride in solvent A, add dropwise to the reaction system, heat up to 60-80°C, react for 8-24 hours, dialyze the reaction solution, and freeze-dry to obtain the solid product quaternized carboxyalkyl chitosan;
4)改性聚乙二醇单甲醚与季铵化羧烷基壳聚糖反应:将步骤3)制备的季铵化羧烷基壳聚糖溶于溶剂B中,再将步骤1)制得的醛化改性聚乙二醇单甲醚采用溶剂B溶解后滴加到反应体系中,加入适量碱液调节溶液pH值在一定范围内,再加入一定量的还原剂,升温至50~80℃,恒温反应6~12h,反应液经分离纯化后,冷冻干燥得最终产物聚乙二醇单甲醚接枝的季铵化羧烷基壳聚糖。4) Reaction of modified polyethylene glycol monomethyl ether with quaternized carboxyalkyl chitosan: dissolve the quaternized carboxyalkyl chitosan prepared in step 3) in solvent B, and then dissolve the quaternized carboxyalkyl chitosan prepared in step 1) The obtained hydroformylated modified polyethylene glycol monomethyl ether is dissolved in solvent B and added dropwise to the reaction system, adding an appropriate amount of lye to adjust the pH value of the solution within a certain range, then adding a certain amount of reducing agent, and raising the temperature to 50~ 80° C., constant temperature reaction for 6-12 hours, the reaction liquid is separated and purified, and freeze-dried to obtain the final product of quaternized carboxyalkyl chitosan grafted with polyethylene glycol monomethyl ether.
按上述方案,优选地,步骤1)中所述醛基化改性的具体步骤为:将1摩尔份聚乙二醇单甲醚溶于一定量的溶剂C中,保持反应在惰性气体环境中,室温不断搅拌条件下加入5~20份醛基化试剂,升温至15~35℃,恒温反应5~15h,将反应液分离纯化后,真空干燥得到醛化聚乙二醇单甲醚;其中,所述聚乙二醇单甲醚的数均分子质量为350、500、750、1000、1900或5000。优选地,所述溶剂C为二氯甲烷、三氯甲烷、二甲亚砜、乙醚中的一种或多种。优选地,所述醛基化试剂为乙酸酐。优选地,惰性气体环境为氮气或氩气。优选地,所述分离纯化为将反应液加入到无水乙醚中,得到的沉淀用氯仿溶解再用乙醚溶液重结晶并重复此步骤一次。According to the above scheme, preferably, the specific steps of the formylation modification described in step 1) are: dissolving 1 mole part of polyethylene glycol monomethyl ether in a certain amount of solvent C, and keeping the reaction in an inert gas environment , add 5-20 parts of formylation reagent under the condition of constant stirring at room temperature, raise the temperature to 15-35°C, react at constant temperature for 5-15 hours, separate and purify the reaction solution, and dry it in vacuum to obtain formylated polyethylene glycol monomethyl ether; , the number average molecular weight of the polyethylene glycol monomethyl ether is 350, 500, 750, 1000, 1900 or 5000. Preferably, the solvent C is one or more of dichloromethane, chloroform, dimethyl sulfoxide, and ether. Preferably, the formylation reagent is acetic anhydride. Preferably, the inert gas environment is nitrogen or argon. Preferably, the separation and purification is to add the reaction solution into anhydrous ether, dissolve the obtained precipitate with chloroform and then recrystallize with ether solution, and repeat this step once.
按上述方案,优选地,步骤2)中,所述N,N-二甲基烷基胺与环氧氯丙烷的质量份数比为1.93~2.97:3.7。According to the above scheme, preferably, in step 2), the ratio of N,N-dimethylalkylamine to epichlorohydrin in parts by mass is 1.93-2.97:3.7.
按上述方案,优选地,步骤2)中,所述的分离纯化为用丙酮淋洗后真空干燥。According to the above scheme, preferably, in step 2), the separation and purification is rinsing with acetone and then vacuum drying.
按上述方案,优选地,步骤3)中所述的羧烷基壳聚糖的制备方法是:According to the foregoing scheme, preferably, the preparation method of the carboxyalkyl chitosan described in step 3) is:
按重量份,将1.61份壳聚糖溶胀,采用碱液调节悬浮液为碱性,在-15℃~-25℃条件下过夜搅拌,加入7.4~14.8份羧基化试剂氯代烷基酸钠,升温到30~60℃搅拌反应3~12h,将反应产物分离纯化,冷冻干燥得到羧烷基壳聚糖;其中,所述氯代烷基酸钠的碳链长度为C2-C10。优选地,所述分离纯化具体为:过滤,将得到的固体产品用80%乙醇和无水乙醇分别漂洗后,于60℃干燥一天,再将固体溶于水后透析。In parts by weight, 1.61 parts of chitosan were swelled, and the suspension was adjusted to be alkaline with lye, stirred overnight at -15°C to -25°C, and 7.4 to 14.8 parts of carboxylation reagent sodium chloroalkylate were added, The temperature is raised to 30-60° C., stirred and reacted for 3-12 hours, the reaction product is separated and purified, and freeze-dried to obtain carboxyalkyl chitosan; wherein, the carbon chain length of the sodium chloroalkylate is C 2 -C 10 . Preferably, the separation and purification specifically include: filtering, rinsing the obtained solid product with 80% ethanol and absolute ethanol respectively, drying at 60° C. for one day, dissolving the solid in water and dialysis.
按上述方案,优选地,步骤3)中,所述的羧烷基壳聚糖与缩水甘油基二甲基烷基氯化铵的质量份数比为3.21:1.93~7.7。According to the above scheme, preferably, in step 3), the ratio of carboxyalkyl chitosan to glycidyl dimethyl alkyl ammonium chloride in parts by mass is 3.21:1.93˜7.7.
按上述方案,优选地,步骤3)中,在将羧烷基壳聚糖采用溶剂A溶解并采用碱液调节溶液pH值后,再将该溶液升温至45~50℃,恒温反应1h。此步骤的作用是让羧烷基壳聚糖链充分打开,接枝更加均匀。According to the above scheme, preferably, in step 3), after dissolving the carboxyalkyl chitosan with solvent A and adjusting the pH value of the solution with lye, the temperature of the solution is raised to 45-50° C., and the reaction is performed at constant temperature for 1 hour. The effect of this step is to fully open the carboxyalkyl chitosan chain, and the grafting is more uniform.
按上述方案,优选地,步骤3)中,所述pH值范围为8~10。According to the above scheme, preferably, in step 3), the pH range is 8-10.
按上述方案,优选地,步骤4)中,所述pH值范围为5~7。According to the above scheme, preferably, in step 4), the pH range is 5-7.
按上述方案,优选地,步骤4)中,所述的季铵化羧烷基壳聚糖、醛化改性聚乙二醇单甲醚以及还原剂的质量份数比为:(0.47~1.05):(0.35~5):(0.08~0.183)。According to the above scheme, preferably, in step 4), the mass fraction ratio of the quaternized carboxyalkyl chitosan, the formaldehyde modified polyethylene glycol monomethyl ether and the reducing agent is: (0.47~1.05 ): (0.35~5): (0.08~0.183).
按上述方案,优选地,步骤4)中,所述还原剂包括但不限于硼氢化钠或氰基硼氢化钠。According to the above scheme, preferably, in step 4), the reducing agent includes but not limited to sodium borohydride or sodium cyanoborohydride.
按上述方案,优选地,所述溶剂A为蒸馏水、异丙醇、氢氧化钠溶液、盐酸溶液,N,N二甲基甲酰胺、N,N二甲基乙酰胺、二甲亚砜、醋酸、甲醇中一种或多种的混合。According to the above scheme, preferably, the solvent A is distilled water, isopropanol, sodium hydroxide solution, hydrochloric acid solution, N,N dimethylformamide, N,N dimethylacetamide, dimethyl sulfoxide, acetic acid , One or more mixtures in methanol.
按上述方案,优选地,所述溶剂B为蒸馏水,异丙醇、碳酸钠水溶液、N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、醋酸、乙醇、甲醇、丙酮、饱和硫酸铵溶液中的一种或多种。According to the above scheme, preferably, the solvent B is distilled water, isopropanol, sodium carbonate aqueous solution, N,N-dimethylformamide, N,N-dimethylacetamide, acetic acid, ethanol, methanol, acetone, One or more of saturated ammonium sulfate solution.
按上述方案,优选地,各步骤中,所述的碱液均为氢氧化钠、氢氧化钾、碳酸钠、碳酸钾中的一种或多种。According to the above scheme, preferably, in each step, the lye is one or more of sodium hydroxide, potassium hydroxide, sodium carbonate, and potassium carbonate.
本发明的合成路线如下:The synthetic route of the present invention is as follows:
1、聚乙二醇单甲醚改性:1. Polyethylene glycol monomethyl ether modification:
2、缩水甘油基二甲基烷基氯化铵制备:2. Preparation of glycidyl dimethyl alkyl ammonium chloride:
3、壳聚糖羧烷基化改性,季铵化改性产物与改性聚乙二醇单甲醚反应:3. Carboxyalkylation modification of chitosan, reaction of quaternized modified product with modified polyethylene glycol monomethyl ether:
现有技术中,传统的聚醚型破乳剂通常以环氧乙烷、环氧丙烷为主要原料,选择具有活泼氢的物质为起始剂,通过聚合醚化得到嵌段聚醚破乳剂;随着油田开采进入后期,大量化合物驱在开采过程中大量使用,此过程加剧了原油乳化程度、增加破乳的难度,嵌段聚醚破乳剂的破乳性能有限。In the prior art, traditional polyether demulsifiers usually use ethylene oxide and propylene oxide as the main raw materials, select substances with active hydrogen as initiators, and obtain block polyether demulsifiers through polymerization etherification; As oilfield development enters the later stage, a large number of compound flooding is widely used in the production process. This process intensifies the degree of emulsification of crude oil and increases the difficulty of demulsification. The demulsification performance of block polyether demulsifiers is limited.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1)本发明以壳聚糖类天然高分子化合物为原料,具有来源广泛、天然、无毒、生物可降解性和兼容性、可持续、使用安全性好等诸多优点。1) The present invention uses chitosan natural polymer compound as raw material, which has many advantages such as wide source, natural, non-toxic, biodegradable and compatible, sustainable and safe to use.
2)通过聚乙二醇单甲醚,氯烷基酸钠,缩水甘油基二甲基烷基氯化铵的改性得到的壳聚糖改性破乳剂具有分子量高、多支链、梳状结构,侧链中羧烷基和二甲基烷基氯化铵对金属阳离子和环烷酸根等带负电的离子及表面呈负电性的颗粒有很强的结合能力,因此本发明方法得到的聚乙二醇单甲醚接枝的季铵化羧烷基壳聚糖具有很好的脱水脱盐效果。2) The modified chitosan demulsifier obtained by modifying polyethylene glycol monomethyl ether, sodium chloroalkylate, and glycidyl dimethyl alkyl ammonium chloride has high molecular weight, multi-branched, comb-like structure, carboxyalkyl and dimethyl alkylammonium chloride in the side chain have very strong binding ability to negatively charged ions such as metal cations and naphthenate radicals and the particles that are negatively charged on the surface, so the poly The quaternized carboxyalkyl chitosan grafted with ethylene glycol monomethyl ether has good dehydration and desalination effects.
3)本发明中,在制备羧烷基壳聚糖时,通过低温碱化的方法,能使壳聚糖分子中氢键更容易被打开,碱液更容易渗透到壳聚糖分子中,进而羧烷基侧链更均匀地接枝到壳聚糖主链上,由此得到的羧烷基壳聚糖结构稳定且溶解性质良好。3) in the present invention, when preparing carboxyalkyl chitosan, by the method for alkalization at low temperature, hydrogen bond in the chitosan molecule can be opened more easily, and lye is more easily penetrated in the chitosan molecule, and then The carboxyalkyl side chains are more uniformly grafted onto the chitosan main chain, and the resulting carboxyalkyl chitosan has a stable structure and good solubility properties.
4)本发明中聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备方法,可通过选择不同碳链长度的羧烷基酸钠,N,N‐二甲基烷基胺,聚醚,或者改变反应原料用量比,或者改变反应体系的反应温度和时间等条件,从而改变破乳剂分子结构如分子量、取代度、疏水链段长度聚集态结构等,进而调控合成的高效破乳剂的脱盐脱水效果,以适用于不同性质(不同产地,含盐含水量不同)的原油。4) The preparation method of polyether grafted chitosan derivative crude oil desalination demulsifier in the present invention can be by selecting sodium carboxyalkylate of different carbon chain lengths, N,N-dimethylalkylamine, polyether, Either change the ratio of raw materials used in the reaction, or change the reaction temperature and time of the reaction system to change the molecular structure of the demulsifier, such as molecular weight, degree of substitution, hydrophobic segment length, aggregated structure, etc., and then regulate the desalination and dehydration of the synthesized high-efficiency demulsifier Effect, so as to be applicable to crude oil with different properties (different origin, different salt and water content).
具体实施方式detailed description
为了更好地理解本发明,下面结合实施实例进一步阐明本发明的内容,但本发明的内容不仅仅局限于下面的实例。In order to better understand the present invention, the content of the present invention will be further illustrated below in conjunction with examples, but the content of the present invention is not limited to the following examples.
实施例1Example 1
一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备,具体步骤如下:A kind of preparation of polyether grafted chitosan derivative crude oil desalination demulsifier, concrete steps are as follows:
(1)聚乙二醇单甲醚端羟基的醛基化改性:取1.75g(5mmol)聚乙二醇单甲醚(Mn=350)溶于30mL无水二甲亚砜和2mL氯仿的混合溶液中,保持反应在氮气环境中,室温下不断搅拌条件下加入5.1mL(50mmol)乙酸酐溶液,加热至15℃,恒温反应5h。反应完成后将反应液加入到400mL无水乙醚中,得到的沉淀用氯仿溶解再用乙醚溶液重结晶(重复此步骤一次),再在室温下真空干燥24h得到醛化聚乙二醇单甲醚。(1) Formylation modification of polyethylene glycol monomethyl ether terminal hydroxyl group: take 1.75g (5mmol) polyethylene glycol monomethyl ether (Mn=350) and dissolve it in 30mL of anhydrous dimethyl sulfoxide and 2mL of chloroform In the mixed solution, keep the reaction under nitrogen atmosphere, add 5.1mL (50mmol) acetic anhydride solution under constant stirring at room temperature, heat to 15°C, and react at constant temperature for 5h. After the reaction was completed, the reaction liquid was added to 400 mL of anhydrous ether, and the obtained precipitate was dissolved in chloroform and then recrystallized with ether solution (repeat this step once), and then vacuum-dried at room temperature for 24 hours to obtain the hydroformylated polyethylene glycol monomethyl ether .
(2)缩水甘油基二甲基十二烷基氯化铵制备:向装有搅拌器,滴液漏斗和冷凝回流装置的三口烧瓶中加入2.13g十二烷基二甲基叔胺,不断搅拌,取3.7g环氧氯丙烷通过滴液漏斗在30min内滴加完成,保持温度25℃,恒温反应6h。停止反应,产物用丙酮淋洗,真空干燥,得到缩水甘油基二甲基十二烷基氯化铵。(2) Preparation of glycidyl dimethyl dodecyl ammonium chloride: add 2.13g of dodecyl dimethyl tertiary amine to the three-necked flask equipped with agitator, dropping funnel and condensation reflux device, constantly stir , take 3.7g of epichlorohydrin through the dropping funnel and add it dropwise within 30min, keep the temperature at 25°C, and react at constant temperature for 6h. Stop the reaction, rinse the product with acetone, and dry it in vacuum to obtain glycidyl dimethyl dodecyl ammonium chloride.
(3)羧甲基壳聚糖的制备:将1.61g壳聚糖加入到250mL的烧瓶中,加入10mL异丙醇溶胀,加入2.5mL 10mol/L的氢氧化钠溶液,继续搅拌30min,在‐15℃条件下过夜搅拌,加入7.4g氯乙酸钠,完全加完后加热反应混合液到60℃并继续搅拌反应3h。反应完成后过滤反应混合物得到粗产品,产品用80%乙醇和无水乙醇分别洗涤3次,放入60℃的干燥箱中干燥一天后,将固体溶于水透析3天,冷冻干燥得N,O‐羧甲基壳聚糖。(3) Preparation of carboxymethyl chitosan: Add 1.61g chitosan to a 250mL flask, add 10mL isopropanol to swell, add 2.5mL 10mol/L sodium hydroxide solution, continue stirring for 30min, and Stir overnight at 15°C, add 7.4g of sodium chloroacetate, heat the reaction mixture to 60°C after the addition is complete, and continue stirring for 3h. After the reaction was completed, the reaction mixture was filtered to obtain a crude product. The product was washed three times with 80% ethanol and absolute ethanol, and dried in a drying oven at 60° C. for one day. The solid was dissolved in water and dialyzed for 3 days, and freeze-dried to obtain N, O‐carboxymethyl chitosan.
(4)季铵化羧甲基壳聚糖的制备:称取3.21g N,O‐羧甲基壳聚糖于三口烧瓶中,加入40mL蒸馏水,用氢氧化钠溶液调节pH=8~10,升温到50℃,恒温反应1h;将2.78g缩水甘油基十二烷基氯化铵溶于20mL水中通过恒压漏斗滴加到反应体系中,升温80℃,反应8h。反应完成后,将反应液透析3~5天,冷冻干燥得到固体产物季铵化羧甲基壳聚糖。(4) Preparation of quaternized carboxymethyl chitosan: Weigh 3.21g of N,O‐carboxymethyl chitosan in a three-necked flask, add 40mL of distilled water, and adjust pH=8~10 with sodium hydroxide solution, Raise the temperature to 50°C, and react at a constant temperature for 1 hour; dissolve 2.78g of glycidyl dodecyl ammonium chloride in 20mL of water and drop it into the reaction system through a constant pressure funnel, raise the temperature to 80°C, and react for 8 hours. After the reaction is completed, the reaction solution is dialyzed for 3 to 5 days, and freeze-dried to obtain a solid product of quaternized carboxymethyl chitosan.
(5)改性聚乙二醇单甲醚与季铵化羧甲基壳聚糖反应:取0.47g季铵化羧甲基壳聚糖置于250mL三口烧瓶中,加入30mL水溶解,将0.4g醛基化聚乙二醇单甲醚(Mn=350)溶于10mL水中,加入适量碳酸钾调节溶液PH=6,再加入0.08g硼氢化钠,10min内滴加完成,搅拌升温至50℃,恒温反应6h。将反应液倒入饱和硫酸铵溶液中沉淀,抽滤,滤液冷冻干燥后用乙醇和丙酮洗涤几次后真空干燥即得目标产物—聚乙二醇单甲醚接枝的季铵化羧甲基壳聚糖,为破乳剂1。(5) Reaction of modified polyethylene glycol monomethyl ether and quaternized carboxymethyl chitosan: take 0.47g of quaternized carboxymethyl chitosan and place it in a 250mL three-necked flask, add 30mL water to dissolve, and dissolve 0.4 Dissolve 1 g of formylated polyethylene glycol monomethyl ether (Mn=350) in 10 mL of water, add an appropriate amount of potassium carbonate to adjust the pH of the solution to 6, then add 0.08 g of sodium borohydride, dropwise add within 10 min, stir and heat up to 50°C , constant temperature reaction 6h. Pour the reaction solution into a saturated ammonium sulfate solution to precipitate, filter with suction, wash the filtrate several times with ethanol and acetone, and then dry it in vacuum to obtain the target product—quaternized carboxymethyl grafted with polyethylene glycol monomethyl ether Chitosan, as demulsifier 1.
实施例2Example 2
一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备,具体步骤如下:A kind of preparation of polyether grafted chitosan derivative crude oil desalination demulsifier, concrete steps are as follows:
(1)聚乙二醇单甲醚端羟基的醛基化改性:取聚乙二醇单甲醚(Mn=750)3.75g(5mmol)溶于30mL无水二甲亚砜和2mL氯仿的混合溶液中,保持反应在氮气环境中,室温下不断搅拌条件下加入5.1mL(50mmol)乙酸酐溶液,加热至20℃,恒温反应7h。反应完成后将反应液加入到400mL无水乙醚中,得到的沉淀用氯仿溶解再用乙醚溶液重结晶(重复此步骤一次),再在室温下真空干燥24h得到醛化聚乙二醇单甲醚。(1) Formylation modification of polyethylene glycol monomethyl ether terminal hydroxyl group: take polyethylene glycol monomethyl ether (Mn=750) 3.75g (5mmol) and dissolve in 30mL of anhydrous dimethyl sulfoxide and 2mL of chloroform In the mixed solution, keep the reaction under nitrogen atmosphere, add 5.1mL (50mmol) acetic anhydride solution under constant stirring at room temperature, heat to 20°C, and react at constant temperature for 7h. After the reaction was completed, the reaction liquid was added to 400 mL of anhydrous ether, and the obtained precipitate was dissolved in chloroform and then recrystallized with ether solution (repeat this step once), and then vacuum-dried at room temperature for 24 hours to obtain the hydroformylated polyethylene glycol monomethyl ether .
(2)缩水甘油基二甲基十四烷基氯化铵制备:向装有搅拌器,滴液漏斗和冷凝回流装置的三口烧瓶中加入2.41g十四烷基二甲基叔胺,不断搅拌,取3.7g环氧氯丙烷通过滴液漏斗在30min内滴加完成,保持温度30℃,恒温反应20h。停止反应,产物用丙酮淋洗,真空干燥,得到缩水甘油基二甲基十四烷基氯化铵。(2) Preparation of glycidyl dimethyltetradecyl ammonium chloride: add 2.41g tetradecyl dimethyl tertiary ammonium to a three-necked flask equipped with a stirrer, dropping funnel and condensing reflux device, constantly stir , take 3.7g of epichlorohydrin through the dropping funnel and add it dropwise within 30min, keep the temperature at 30°C, and react at constant temperature for 20h. The reaction was stopped, and the product was rinsed with acetone and dried in vacuo to obtain glycidyl dimethyltetradecyl ammonium chloride.
(3)羧乙基壳聚糖的制备:将1.61g壳聚糖加入到250mL的烧瓶中,加入10mL异丙醇溶胀,加入2.5mL 10mol/L的氢氧化钠溶液,继续搅拌30min,在-20℃条件下过夜搅拌,加入8.2g氯丙酸钠,完全加完后加热反应混合液到60℃并继续搅拌反应4h。反应完成后过滤反应混合物得到固体产品,产品用80%乙醇和无水乙醇分别洗涤3次,放入60℃的干燥箱中干燥,再将固体溶于水后透析5天,冷冻干燥得固体产品N,O-羧乙基壳聚糖。(3) Preparation of carboxyethyl chitosan: Add 1.61g chitosan to a 250mL flask, add 10mL isopropanol to swell, add 2.5mL 10mol/L sodium hydroxide solution, continue stirring for 30min, and Stir overnight at 20°C, add 8.2g of sodium chloropropionate, heat the reaction mixture to 60°C after the addition is complete, and continue stirring for 4 hours. After the reaction is completed, filter the reaction mixture to obtain a solid product. The product is washed three times with 80% ethanol and absolute ethanol respectively, put into a drying oven at 60°C for drying, then dissolve the solid in water, dialyze for 5 days, and freeze-dry to obtain a solid product. N,O-carboxyethyl chitosan.
(4)季铵化羧乙基壳聚糖的制备:称取3.21g N,O-羧乙基壳聚糖于三口烧瓶中,加入40mL蒸馏水,用氢氧化钠溶液调节pH=8~10,升温到45℃,恒温反应1h。将2.78g缩水甘油基十四烷基氯化铵溶于20mL水中通过恒压漏斗滴加到反应体系中,升温到70℃,反应16h。反应完成后,反应液透析5天,冷冻干燥得到固体产物季铵化羧乙基壳聚糖。(4) Preparation of quaternized carboxyethyl chitosan: Weigh 3.21g of N,O-carboxyethyl chitosan in a three-neck flask, add 40mL of distilled water, adjust pH=8~10 with sodium hydroxide solution, The temperature was raised to 45°C, and the reaction was performed at a constant temperature for 1h. Dissolve 2.78g of glycidyltetradecylammonium chloride in 20mL of water and add dropwise to the reaction system through a constant pressure funnel, raise the temperature to 70°C, and react for 16h. After the reaction was completed, the reaction solution was dialyzed for 5 days, and freeze-dried to obtain a solid product, quaternized carboxyethyl chitosan.
(5)改性聚乙二醇单甲醚与季铵化羧乙基壳聚糖反应:取0.53g季铵化羧乙基壳聚糖置于250mL三口烧瓶中,加入30mL水溶解,将0.8g醛基化聚乙二醇单甲醚(Mn=750)溶于10mL水中,加入适量碳酸钾调节溶液PH=6,再加入0.16g硼氢化钠,10min内滴加完成,搅拌升温至65℃,恒温反应7h。将反应液倒入饱和硫酸铵溶液中沉淀,抽滤,滤液冷冻干燥后用乙醇和丙酮洗涤几次后真空干燥即得目标产物—聚乙二醇单甲醚接枝的季铵化羧乙基壳聚糖,为破乳剂2。(5) Reaction of modified polyethylene glycol monomethyl ether with quaternized carboxyethyl chitosan: take 0.53g of quaternized carboxyethyl chitosan and place it in a 250mL three-necked flask, add 30mL water to dissolve, and dissolve 0.8 Dissolve 1 g of formylated polyethylene glycol monomethyl ether (Mn=750) in 10 mL of water, add an appropriate amount of potassium carbonate to adjust the pH of the solution to 6, then add 0.16 g of sodium borohydride, dropwise add within 10 min, stir and heat up to 65°C , constant temperature reaction 7h. Pour the reaction solution into a saturated ammonium sulfate solution to precipitate, filter with suction, wash the filtrate several times with ethanol and acetone, and then dry it in vacuum to obtain the target product—quaternized carboxyethyl grafted with polyethylene glycol monomethyl ether Chitosan, as demulsifier 2.
实施例3Example 3
一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备,具体步骤如下:A kind of preparation of polyether grafted chitosan derivative crude oil desalination demulsifier, concrete steps are as follows:
(1)聚乙二醇单甲醚端羟基的醛基化改性:取聚乙二醇单甲醚(Mn=1000)5g(5mmol)溶于30mL无水二甲亚砜和2mL氯仿的混合溶液中,保持反应在氮气环境中,室温下不断搅拌条件下加入5.1mL(50mmol)乙酸酐溶液,升温至30℃,恒温反应时间为9h。反应完成后将反应液加入到400mL无水乙醚中,得到的沉淀用氯仿溶解再用乙醚溶液重结晶(重复此步骤一次),再在室温下真空干燥24h得到醛化聚乙二醇单甲醚。(1) Formylation modification of polyethylene glycol monomethyl ether terminal hydroxyl group: take polyethylene glycol monomethyl ether (Mn=1000) 5g (5mmol) and dissolve in 30mL of anhydrous dimethyl sulfoxide and 2mL of chloroform In the solution, keep the reaction under nitrogen atmosphere, add 5.1mL (50mmol) acetic anhydride solution under constant stirring at room temperature, raise the temperature to 30°C, and keep the reaction time at constant temperature for 9h. After the reaction was completed, the reaction liquid was added to 400 mL of anhydrous ether, and the obtained precipitate was dissolved in chloroform and then recrystallized with ether solution (repeat this step once), and then vacuum-dried at room temperature for 24 hours to obtain the hydroformylated polyethylene glycol monomethyl ether .
(2)缩水甘油基二甲基十六烷基氯化铵制备:向装有搅拌器,滴液漏斗和冷凝回流装置的三口烧瓶中加入2.69g十六烷基二甲基叔胺,不断搅拌,取3.7g环氧氯丙烷并用滴液漏斗在30min内滴加完成,保持温度40℃,恒温反应30h后,停止反应。产物用丙酮洗涤,真空干燥,得到缩水甘油基二甲基十六烷基氯化铵。(2) Preparation of glycidyl dimethyl cetyl ammonium chloride: add 2.69g cetyl dimethyl tertiary amine to a three-necked flask equipped with a stirrer, dropping funnel and condensation reflux device, constantly stir , Take 3.7g of epichlorohydrin and use the dropping funnel to drop it within 30min, keep the temperature at 40°C, and stop the reaction after constant temperature reaction for 30h. The product was washed with acetone and dried in vacuo to obtain glycidyl dimethyl hexadecyl ammonium chloride.
(3)羧丙基壳聚糖的制备:将1.61g壳聚糖加入到250mL的烧瓶中,加入10mL异丙醇溶胀,加入2.5mL 10mol/L的氢氧化钠溶液,继续搅拌30min,在-25℃条件下过夜搅拌,加入9.5g氯丁酸钠,完全加完后加热反应混合液到30℃并继续搅拌反应12h。反应完成后过滤反应混合物得到固体产品,产品用80%乙醇和无水乙醇分别洗涤3次,放入60℃的干燥箱中干燥,再将固体溶于水后透析4天,冷冻干燥得固体产品N,O-羧丙基壳聚糖。(3) Preparation of carboxypropyl chitosan: join 1.61g chitosan in 250mL flask, add 10mL isopropanol to swell, add 2.5mL 10mol/L sodium hydroxide solution, continue to stir for 30min, in- Stir overnight at 25°C, add 9.5g of sodium chlorobutyrate, heat the reaction mixture to 30°C after the addition is complete, and continue stirring for 12 hours. After the reaction was completed, the reaction mixture was filtered to obtain a solid product. The product was washed three times with 80% ethanol and absolute ethanol, and dried in a drying oven at 60°C. The solid was dissolved in water, dialyzed for 4 days, and freeze-dried to obtain a solid product. N,O-carboxypropyl chitosan.
(4)季铵化羧丙基壳聚糖的制备:称取3.21g N,O-羧丙基壳聚糖于三口烧瓶中,加入40mL蒸馏水,用氢氧化钠溶液调节pH=8~10,升温到45℃,恒温反应1h。将2.86g缩水甘油基二甲基十六烷基氯化铵溶于20mL水中通过恒压漏斗滴加到反应体系中,升温到60℃,反应24h。反应完成后,反应液透析5天,冷冻干燥得到固体产物季铵化羧丙基壳聚糖。(4) Preparation of quaternized carboxypropyl chitosan: Weigh 3.21g of N,O-carboxypropyl chitosan in a three-necked flask, add 40mL of distilled water, adjust pH=8~10 with sodium hydroxide solution, The temperature was raised to 45°C, and the reaction was performed at a constant temperature for 1h. Dissolve 2.86g of glycidyl dimethyl hexadecyl ammonium chloride in 20mL of water and add dropwise to the reaction system through a constant pressure funnel, raise the temperature to 60°C, and react for 24h. After the reaction was completed, the reaction solution was dialyzed for 5 days, and freeze-dried to obtain a solid product, quaternized carboxypropyl chitosan.
(5)改性聚乙二醇单甲醚与季铵化羧丙基壳聚糖反应:取0.64g季铵化羧丙基壳聚糖置于250mL三口烧瓶中,加入30mL水溶解,将1.1g醛基化聚乙二醇单甲醚(Mn=1000)溶于10mL水中,加入适量碳酸钾调节溶液PH=6,再加入0.183g硼氢化钠,10min内滴加完成,搅拌升温至80℃,恒温反应8h。将反应液倒入饱和硫酸铵溶液中沉淀,抽滤,滤液冷冻干燥后用乙醇和丙酮洗涤几次后真空干燥即得目标产物—聚乙二醇单甲醚接枝的季铵化羧丙基壳聚糖,为破乳剂3。(5) Reaction of modified polyethylene glycol monomethyl ether and quaternized carboxypropyl chitosan: take 0.64g of quaternized carboxypropyl chitosan and place it in a 250mL three-necked flask, add 30mL water to dissolve, and dissolve 1.1 Dissolve 1 g of formylated polyethylene glycol monomethyl ether (Mn=1000) in 10 mL of water, add an appropriate amount of potassium carbonate to adjust the pH of the solution to 6, then add 0.183 g of sodium borohydride, drop it within 10 minutes, stir and heat up to 80°C , constant temperature reaction 8h. Pour the reaction solution into a saturated ammonium sulfate solution to precipitate, filter with suction, wash the filtrate several times with ethanol and acetone, and then dry it in vacuum to obtain the target product—quaternized carboxypropyl grafted with polyethylene glycol monomethyl ether Chitosan, as demulsifier3.
实施例4Example 4
一种聚醚接枝壳聚糖衍生物原油脱盐破乳剂的制备,具体步骤如下:A kind of preparation of polyether grafted chitosan derivative crude oil desalination demulsifier, concrete steps are as follows:
(1)聚乙二醇单甲醚端羟基的醛基化改性:取聚乙二醇单甲醚(Mn=5000)5g(1mmol)溶于30mL无水二甲亚砜和氯仿2mL的混合溶液中,保持反应在氮气环境中,室温下不断搅拌条件下加入1.1mL(10mmol)乙酸酐溶液,升温至35℃,恒温反应15h。反应完成后将反应液加入到400mL无水乙醚中,得到的沉淀用氯仿溶解再用乙醚溶液重结晶(重复此步骤一次),再在室温下真空干燥24h得到醛化聚乙二醇单甲醚。(1) Formylation modification of polyethylene glycol monomethyl ether terminal hydroxyl group: Take polyethylene glycol monomethyl ether (Mn=5000) 5g (1mmol) and dissolve it in 30mL of anhydrous dimethyl sulfoxide and chloroform 2mL In the solution, keep the reaction under nitrogen atmosphere, add 1.1mL (10mmol) acetic anhydride solution under constant stirring at room temperature, raise the temperature to 35°C, and react at constant temperature for 15h. After the reaction was completed, the reaction liquid was added to 400 mL of anhydrous ether, and the obtained precipitate was dissolved in chloroform and then recrystallized with ether solution (repeat this step once), and then vacuum-dried at room temperature for 24 hours to obtain the hydroformylated polyethylene glycol monomethyl ether .
(2)缩水甘油基二甲基三十二烷基氯化铵制备:向装有搅拌器,滴液漏斗和冷凝回流装置的三口烧瓶中加入2.97g三十二烷基二甲基叔胺,不断搅拌,取3.7g环氧氯丙烷通过滴液漏斗在30min内滴加完成,保持温度40℃,恒温反应30h。停止反应,产物用丙酮淋洗,真空干燥,得到缩水甘油基二甲基三十二烷基氯化铵。(2) Preparation of glycidyl dimethyl docosyl ammonium chloride: add 2.97g docosyl dimethyl tertiary amine to the three-necked flask equipped with agitator, dropping funnel and condensing reflux device, Stir continuously, take 3.7g of epichlorohydrin through the dropping funnel and add dropwise within 30min, keep the temperature at 40°C, and react at constant temperature for 30h. The reaction was stopped, and the product was rinsed with acetone and dried in vacuo to obtain glycidyl dimethyl tridodecyl ammonium chloride.
(3)羧壬基壳聚糖的制备:将1.61g壳聚糖加入到250mL的烧瓶中,加入10mL异丙醇溶胀,加入2.5mL 10mol/L的氢氧化钠溶液,继续搅拌30min,在-20℃条件下过夜搅拌,加入14.8g氯癸酸钠,完全加完后加热反应混合液到60℃并继续搅拌反应3h。反应完成后过滤反应混合物得到粗产品,产品用80%乙醇和无水乙醇分别洗涤3次,放入60℃的干燥箱中干燥一天后,将固体溶于水透析3天,冷冻干燥得N,O-羧壬基壳聚糖。(3) Preparation of carboxynonyl chitosan: Add 1.61g of chitosan to a 250mL flask, add 10mL of isopropanol to swell, add 2.5mL of 10mol/L sodium hydroxide solution, continue stirring for 30min, and Stir overnight at 20°C, add 14.8g of sodium chlorodecanoate, heat the reaction mixture to 60°C after the addition is complete, and continue stirring for 3h. After the reaction was completed, the reaction mixture was filtered to obtain a crude product. The product was washed three times with 80% ethanol and absolute ethanol, and dried in a drying oven at 60° C. for one day. The solid was dissolved in water and dialyzed for 3 days, and freeze-dried to obtain N, O-carboxynonyl chitosan.
(4)季铵化羧壬基壳聚糖的制备:称取3.21g N,O-羧甲基壳聚糖于三口烧瓶中,加入40mL二甲亚砜,用氢氧化钠溶液调节pH=8~10,升温到50℃,恒温反应1h(让羧甲基壳聚糖链充分打开,接枝更加均匀);将7.7g缩水甘油基三十二烷基氯化铵溶于20mL二甲亚砜中,通过恒压漏斗滴加到反应体系中,升温80℃,反应8h。反应完成后,将反应液透析3~5天,冷冻干燥得到固体产物季铵化羧壬基壳聚糖。(4) Preparation of quaternized carboxynonyl chitosan: Weigh 3.21g N,O-carboxymethyl chitosan in a three-necked flask, add 40mL dimethyl sulfoxide, and adjust pH=8 with sodium hydroxide solution ~10°C, heat up to 50°C, and react at a constant temperature for 1h (to allow the carboxymethyl chitosan chain to fully open and the grafting to be more uniform); Add it dropwise to the reaction system through a constant pressure funnel, raise the temperature to 80°C, and react for 8 hours. After the reaction is completed, the reaction liquid is dialyzed for 3 to 5 days, and freeze-dried to obtain a solid product of quaternized carboxynonyl chitosan.
(5)改性聚乙二醇单甲醚与季铵化羧壬基壳聚糖反应:取1.05g季铵化羧壬基壳聚糖置于250mL三口烧瓶中,加入30mL水溶解,将5g醛基化聚乙二醇单甲醚(Mn=5000)溶于10mL水中,加入适量碳酸钾调节溶液PH=6,再加入0.183g硼氢化钠,10min内滴加完成,搅拌升温至65℃,恒温反应8h。将反应液倒入饱和硫酸铵溶液中沉淀,抽滤,滤液冷冻干燥后用乙醇和丙酮洗涤几次后真空干燥即得目标产物—聚乙二醇单甲醚接枝的季铵化羧壬基壳聚糖,为破乳剂4。(5) Reaction of modified polyethylene glycol monomethyl ether with quaternized carboxynonyl chitosan: take 1.05 g of quaternized carboxynonyl chitosan and place it in a 250 mL three-neck flask, add 30 mL of water to dissolve, and dissolve 5 g Dissolve aldylated polyethylene glycol monomethyl ether (Mn=5000) in 10 mL of water, add an appropriate amount of potassium carbonate to adjust the pH of the solution to 6, then add 0.183 g of sodium borohydride, dropwise within 10 minutes, stir and heat up to 65 °C, Constant temperature reaction 8h. Pour the reaction solution into a saturated ammonium sulfate solution to precipitate, filter with suction, wash the filtrate several times with ethanol and acetone, and then dry it in vacuum to obtain the target product—quaternized carboxynonyl grafted with polyethylene glycol monomethyl ether Chitosan, as demulsifier4.
对比实施例1Comparative Example 1
取实施例1中步骤(4)制得的季铵化羧甲基壳聚糖作为破乳剂对比例1。Get the quaternized carboxymethyl chitosan prepared by step (4) in Example 1 as the demulsifier comparative example 1.
对比实施例2Comparative Example 2
根据中国专利申请CN201310289037.6的公告文本中实施例1的方法制得的一种多糖类天然高分子改性的原油破乳剂作为破乳剂对比例2。A polysaccharide natural polymer modified crude oil demulsifier prepared according to the method of Example 1 in the announcement text of Chinese patent application CN201310289037.6 was used as demulsifier comparative example 2.
对比实施例3Comparative Example 3
以市售的商品牌号为JL系列破乳剂为破乳剂对比例3Taking the commercially available brand name as JL series demulsifier as demulsifier comparative example 3
破乳剂破乳效果实验Demulsifier Demulsification Effect Experiment
以中国石油化工股份有限公司武汉分公司提供的原油作为本发明破乳实验用油进行实验,按GB/T 8929-88(蒸馏法)进行测定,测得原油中水含量为50%。The crude oil provided by Wuhan Branch of China Petroleum & Chemical Corporation was used as the oil for the demulsification experiment of the present invention. It was measured according to GB/T 8929-88 (distillation method), and the water content in the crude oil was measured to be 50%.
设定脱水温度为60~80℃,原油中破乳剂浓度为70~120ppm。参照中华人民共和国石油天然气行业标准SY/T 5281-2000《原油破乳剂使用性能检测方法(瓶试法)》,分别对实施例1-4制得的破乳剂1-4和对比实施例制得的破乳剂对比例1-3的破乳性能进行测试,试验中脱水试瓶的震荡方法采用机械震荡法。Set the dehydration temperature at 60-80°C, and the concentration of demulsifier in crude oil at 70-120ppm. With reference to the Petroleum and Natural Gas Industry Standard SY/T 5281-2000 of the People's Republic of China "Crude Oil Demulsifier Performance Test Method (Bottle Test Method)", the demulsifiers 1-4 and comparative examples prepared in Examples 1-4 were prepared respectively The demulsifier comparative example 1-3 demulsification performance is tested, and the vibration method of dehydration test bottle adopts mechanical vibration method in the test.
具体步骤如下:将原油乳状液样品倒入100mL具塞量筒中,恒温水浴加热30min;用移液管向具塞量筒中加入一定量的原油破乳剂溶液;采用机械震荡法,振幅大于20cm,震荡时间为5min,充分混匀后,将具塞量筒重新置于恒温水浴中静置沉降;开始计时,记录不同时间(5min,15min,30min,60min,120min)的脱水量,终止沉降时,观测记录污水颜色和油水界面状况。The specific steps are as follows: pour the crude oil emulsion sample into a 100mL stoppered measuring cylinder, and heat it in a constant temperature water bath for 30 minutes; add a certain amount of crude oil demulsifier solution into the stoppered measuring cylinder with a pipette; The time is 5 minutes. After fully mixing, put the stoppered measuring cylinder back in the constant temperature water bath and let it settle; start timing, record the dehydration amount at different times (5min, 15min, 30min, 60min, 120min), and observe and record when the settlement is terminated. Sewage color and oil-water interface condition.
实验结果显示,相比于破乳剂对比例1-3,根据本发明方法得到的破乳剂1-4在脱水温度为60~80℃,破乳剂浓度为70~120ppm范围内,均有更好的脱水脱盐效果,尤其在浓度为70ppm、脱水温度为60℃时效果最佳。The experimental results show that, compared with the demulsifier comparative examples 1-3, the demulsifier 1-4 obtained according to the method of the present invention has a better performance when the dehydration temperature is 60-80°C and the demulsifier concentration is 70-120ppm. The effect of dehydration and desalination is the best, especially when the concentration is 70ppm and the dehydration temperature is 60℃.
实施例1-4制备的破乳剂1-4与对比实施例1-3中提供的破乳剂对比例1-3,在上述最佳浓度和温度条件下,破乳脱水实验效果见表1,破乳脱盐实验效果见表2。For the demulsifier 1-4 prepared in Example 1-4 and the demulsifier Comparative Example 1-3 provided in Comparative Example 1-3, under the above-mentioned optimal concentration and temperature conditions, the demulsification and dehydration experiment results are shown in Table 1. The results of the milk desalination experiment are shown in Table 2.
表1Table 1
表2Table 2
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Effective date of registration: 20241107 Address after: 163000 Commercial Service Building A-7, Guangxia Community, Ranghulu District, Daqing City, Heilongjiang Province, China Patentee after: Daqing Changhong Petrochemical Technology Co.,Ltd. Country or region after: China Address before: 430074, No. 693 Xiong Chu street, Hongshan District, Hubei, Wuhan Patentee before: WUHAN INSTITUTE OF TECHNOLOGY Country or region before: China |