CN101182643A - A kind of environment-friendly composite pre-film agent for pre-film treatment of circulating cooling water system and its application method - Google Patents
A kind of environment-friendly composite pre-film agent for pre-film treatment of circulating cooling water system and its application method Download PDFInfo
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- CN101182643A CN101182643A CNA2007101708050A CN200710170805A CN101182643A CN 101182643 A CN101182643 A CN 101182643A CN A2007101708050 A CNA2007101708050 A CN A2007101708050A CN 200710170805 A CN200710170805 A CN 200710170805A CN 101182643 A CN101182643 A CN 101182643A
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- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 170
- 239000000498 cooling water Substances 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 10
- 239000002131 composite material Substances 0.000 title abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 102
- 229920001577 copolymer Polymers 0.000 claims abstract description 33
- QRUDEWIWKLJBPS-UHFFFAOYSA-N benzotriazole Chemical compound C1=CC=C2N[N][N]C2=C1 QRUDEWIWKLJBPS-UHFFFAOYSA-N 0.000 claims abstract description 30
- 239000012964 benzotriazole Substances 0.000 claims abstract description 30
- 229910000368 zinc sulfate Inorganic materials 0.000 claims abstract description 19
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229960001763 zinc sulfate Drugs 0.000 claims abstract description 9
- RZLVQBNCHSJZPX-UHFFFAOYSA-L zinc sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Zn+2].[O-]S([O-])(=O)=O RZLVQBNCHSJZPX-UHFFFAOYSA-L 0.000 claims description 16
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 14
- 239000001273 butane Substances 0.000 claims description 13
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 8
- 238000006116 polymerization reaction Methods 0.000 claims description 2
- 229940074404 sodium succinate Drugs 0.000 claims 3
- ZDQYSKICYIVCPN-UHFFFAOYSA-L sodium succinate (anhydrous) Chemical compound [Na+].[Na+].[O-]C(=O)CCC([O-])=O ZDQYSKICYIVCPN-UHFFFAOYSA-L 0.000 claims 3
- 230000003134 recirculating effect Effects 0.000 claims 2
- GWZMWHWAWHPNHN-UHFFFAOYSA-N 2-hydroxypropyl prop-2-enoate Chemical compound CC(O)COC(=O)C=C GWZMWHWAWHPNHN-UHFFFAOYSA-N 0.000 claims 1
- 239000012467 final product Substances 0.000 claims 1
- 229920001897 terpolymer Polymers 0.000 claims 1
- IPCXNCATNBAPKW-UHFFFAOYSA-N zinc;hydrate Chemical compound O.[Zn] IPCXNCATNBAPKW-UHFFFAOYSA-N 0.000 claims 1
- 238000005260 corrosion Methods 0.000 abstract description 41
- 230000007797 corrosion Effects 0.000 abstract description 39
- 239000011734 sodium Substances 0.000 abstract description 36
- 239000011574 phosphorus Substances 0.000 abstract description 24
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 24
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 20
- 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 abstract description 16
- 229910000365 copper sulfate Inorganic materials 0.000 abstract description 16
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 abstract description 16
- 229910052708 sodium Inorganic materials 0.000 abstract description 16
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 abstract description 16
- 235000015393 sodium molybdate Nutrition 0.000 abstract description 11
- 239000011684 sodium molybdate Substances 0.000 abstract description 11
- 229910000975 Carbon steel Inorganic materials 0.000 abstract description 8
- 239000010962 carbon steel Substances 0.000 abstract description 8
- 239000000126 substance Substances 0.000 abstract description 8
- 239000007788 liquid Substances 0.000 abstract description 7
- 239000012528 membrane Substances 0.000 abstract description 6
- 230000001681 protective effect Effects 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 2
- 150000001735 carboxylic acids Chemical class 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 abstract 1
- 239000002075 main ingredient Substances 0.000 abstract 1
- LRXTYHSAJDENHV-UHFFFAOYSA-H zinc phosphate Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LRXTYHSAJDENHV-UHFFFAOYSA-H 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 description 33
- 239000007787 solid Substances 0.000 description 33
- 238000012360 testing method Methods 0.000 description 27
- 229920001529 polyepoxysuccinic acid Polymers 0.000 description 25
- 238000003756 stirring Methods 0.000 description 25
- IRLPACMLTUPBCL-KQYNXXCUSA-N 5'-adenylyl sulfate Chemical compound C1=NC=2C(N)=NC=NC=2N1[C@@H]1O[C@H](COP(O)(=O)OS(O)(=O)=O)[C@@H](O)[C@H]1O IRLPACMLTUPBCL-KQYNXXCUSA-N 0.000 description 21
- 239000000203 mixture Substances 0.000 description 14
- 230000005764 inhibitory process Effects 0.000 description 12
- 239000003112 inhibitor Substances 0.000 description 11
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 11
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 11
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 10
- 239000011575 calcium Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 10
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 10
- RWVGQQGBQSJDQV-UHFFFAOYSA-M sodium;3-[[4-[(e)-[4-(4-ethoxyanilino)phenyl]-[4-[ethyl-[(3-sulfonatophenyl)methyl]azaniumylidene]-2-methylcyclohexa-2,5-dien-1-ylidene]methyl]-n-ethyl-3-methylanilino]methyl]benzenesulfonate Chemical compound [Na+].C1=CC(OCC)=CC=C1NC1=CC=C(C(=C2C(=CC(C=C2)=[N+](CC)CC=2C=C(C=CC=2)S([O-])(=O)=O)C)C=2C(=CC(=CC=2)N(CC)CC=2C=C(C=CC=2)S([O-])(=O)=O)C)C=C1 RWVGQQGBQSJDQV-UHFFFAOYSA-M 0.000 description 10
- 239000011686 zinc sulphate Substances 0.000 description 10
- 235000009529 zinc sulphate Nutrition 0.000 description 10
- 239000002455 scale inhibitor Substances 0.000 description 9
- 229920000388 Polyphosphate Polymers 0.000 description 8
- 239000001205 polyphosphate Substances 0.000 description 8
- 235000011176 polyphosphates Nutrition 0.000 description 8
- 150000003751 zinc Chemical class 0.000 description 8
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Natural products P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 6
- 238000011161 development Methods 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 6
- YDONNITUKPKTIG-UHFFFAOYSA-N [Nitrilotris(methylene)]trisphosphonic acid Chemical compound OP(O)(=O)CN(CP(O)(O)=O)CP(O)(O)=O YDONNITUKPKTIG-UHFFFAOYSA-N 0.000 description 5
- 239000011248 coating agent Substances 0.000 description 5
- 239000002270 dispersing agent Substances 0.000 description 5
- VPTUPAVOBUEXMZ-UHFFFAOYSA-N (1-hydroxy-2-phosphonoethyl)phosphonic acid Chemical compound OP(=O)(O)C(O)CP(O)(O)=O VPTUPAVOBUEXMZ-UHFFFAOYSA-N 0.000 description 4
- 229940120146 EDTMP Drugs 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- ABLZXFCXXLZCGV-UHFFFAOYSA-N Phosphorous acid Chemical compound OP(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 239000001506 calcium phosphate Substances 0.000 description 4
- 229910000389 calcium phosphate Inorganic materials 0.000 description 4
- 235000011010 calcium phosphates Nutrition 0.000 description 4
- 229940090960 diethylenetriamine pentamethylene phosphonic acid Drugs 0.000 description 4
- DUYCTCQXNHFCSJ-UHFFFAOYSA-N dtpmp Chemical compound OP(=O)(O)CN(CP(O)(O)=O)CCN(CP(O)(=O)O)CCN(CP(O)(O)=O)CP(O)(O)=O DUYCTCQXNHFCSJ-UHFFFAOYSA-N 0.000 description 4
- NFDRPXJGHKJRLJ-UHFFFAOYSA-N edtmp Chemical compound OP(O)(=O)CN(CP(O)(O)=O)CCN(CP(O)(O)=O)CP(O)(O)=O NFDRPXJGHKJRLJ-UHFFFAOYSA-N 0.000 description 4
- 231100000252 nontoxic Toxicity 0.000 description 4
- 230000003000 nontoxic effect Effects 0.000 description 4
- UEZVMMHDMIWARA-UHFFFAOYSA-M phosphonate Chemical compound [O-]P(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-M 0.000 description 4
- 229910000073 phosphorus hydride Inorganic materials 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 4
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 4
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 4
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000012851 eutrophication Methods 0.000 description 3
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical compound [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 3
- -1 phosphine carboxylic acid Chemical class 0.000 description 3
- 229920005646 polycarboxylate Polymers 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 235000019832 sodium triphosphate Nutrition 0.000 description 3
- LMHAGAHDHRQIMB-UHFFFAOYSA-N 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane Chemical compound FC1(F)C(F)(F)C(F)(Cl)C1(F)Cl LMHAGAHDHRQIMB-UHFFFAOYSA-N 0.000 description 2
- QZPSOSOOLFHYRR-UHFFFAOYSA-N 3-hydroxypropyl prop-2-enoate Chemical compound OCCCOC(=O)C=C QZPSOSOOLFHYRR-UHFFFAOYSA-N 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical compound CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 description 2
- 239000010452 phosphate Substances 0.000 description 2
- 229920000058 polyacrylate Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 229920005552 sodium lignosulfonate Polymers 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- CJFGPLRCLIHOMY-UHFFFAOYSA-N 2-hydroxyphosphanylacetic acid Chemical compound OPCC(O)=O CJFGPLRCLIHOMY-UHFFFAOYSA-N 0.000 description 1
- 239000004135 Bone phosphate Substances 0.000 description 1
- 241001677188 Coccus viridis Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229910004619 Na2MoO4 Inorganic materials 0.000 description 1
- 229920000805 Polyaspartic acid Polymers 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- JMTIXSZQYHAMLY-UHFFFAOYSA-N [P].[Zn] Chemical compound [P].[Zn] JMTIXSZQYHAMLY-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- ATMLPEJAVWINOF-UHFFFAOYSA-N acrylic acid acrylic acid Chemical compound OC(=O)C=C.OC(=O)C=C ATMLPEJAVWINOF-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 229920002988 biodegradable polymer Polymers 0.000 description 1
- 239000004621 biodegradable polymer Substances 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- MTNDZQHUAFNZQY-UHFFFAOYSA-N imidazoline Chemical compound C1CN=CN1 MTNDZQHUAFNZQY-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000012669 liquid formulation Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- YACKEPLHDIMKIO-UHFFFAOYSA-N methylphosphonic acid Chemical compound CP(O)(O)=O YACKEPLHDIMKIO-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 108010064470 polyaspartate Proteins 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 150000003852 triazoles Chemical class 0.000 description 1
- PBYZMCDFOULPGH-UHFFFAOYSA-N tungstate Chemical compound [O-][W]([O-])(=O)=O PBYZMCDFOULPGH-UHFFFAOYSA-N 0.000 description 1
- 229940104383 zinc sulfate 80 mg Drugs 0.000 description 1
- MFXMOUUKFMDYLM-UHFFFAOYSA-L zinc;dihydrogen phosphate Chemical compound [Zn+2].OP(O)([O-])=O.OP(O)([O-])=O MFXMOUUKFMDYLM-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
本发明属于循环冷却水处理技术领域,具体涉及一种用于循环冷却水系统预膜处理的环保型复合预膜剂及其使用方法,该环保型复合预膜剂是以2-膦酸基-1,2,4-三羧酸丁烷、聚环氧琥珀酸钠为主要成分,并添加适量的羧酸基共聚物、苯并三氮唑、钼酸钠、硫酸锌等成分而成,使用时将该复合预膜剂直接加入循环冷却水中,运行48小时即可在碳钢表面形成具有防腐蚀功能的保护膜,所形成的膜对硫酸铜标准点滴液的耐蚀性远远优于传统的磷锌预膜剂。该环保型复合预膜剂预膜时总磷含量<7.5mg/L,不需调节水质pH,预膜后水质澄清透明,不需置换水质即可直接转为正常运行,不仅节约了置换用水,而且减少了置换水质后的正常运行时的药剂基础投加费用,同时没有预膜废液的排放,属于环境友好型预膜方法。The invention belongs to the technical field of circulating cooling water treatment, and specifically relates to an environment-friendly composite pre-film agent for pre-film treatment of a circulating cooling water system and a method for using the environment-friendly composite pre-film agent based on 2-phosphonic acid- 1,2,4-Butane tricarboxylate and sodium polyepoxysuccinate are the main ingredients, and an appropriate amount of carboxylic acid-based copolymer, benzotriazole, sodium molybdate, zinc sulfate and other ingredients are added. When the composite pre-film agent is directly added to the circulating cooling water, a protective film with anti-corrosion function can be formed on the surface of carbon steel after 48 hours of operation. The corrosion resistance of the formed film to copper sulfate standard drip solution is far superior to that of traditional Phosphate-zinc pre-film agent. The environmental-friendly composite pre-film agent has a total phosphorus content of less than 7.5mg/L during pre-filming, and does not need to adjust the pH of the water. After pre-filming, the water quality is clear and transparent, and it can be directly converted to normal operation without replacing the water quality. Moreover, it reduces the basic chemical dosing cost during normal operation after the water quality is replaced, and at the same time, there is no discharge of pre-membrane waste liquid, which belongs to an environmentally friendly pre-membrane method.
Description
技术领域technical field
本发明属于循环冷却水处理技术领域,涉及一种用于循环冷却水系统预膜处理的环保型复合预膜剂及其使用方法,具体地说涉及一种用于不加酸、预膜后不置换水质即可直接转为正常运行的循环冷却水系统用环保型复合预膜剂及使用方法。The invention belongs to the technical field of circulating cooling water treatment, and relates to an environment-friendly composite pre-filming agent used for pre-filming treatment of circulating cooling water system and its use method, in particular to a compound pre-filming agent for no acid addition, no pre-filming after pre-filming The replacement water quality can be directly converted into an environment-friendly composite pre-film agent for a circulating cooling water system in normal operation and its usage method.
背景技术Background technique
预膜是工业水处理技术中必不可少的重要环节之一,是提高循环水设备耐蚀能力的一项重要手段,其目的是在化学清洗后的金属表面生成一层致密而耐蚀的保护膜。同一循环冷却水处理配方,是否预膜,直接影响该配方的缓蚀效果,其腐蚀速度最大要差20倍左右。为了提高配方的缓蚀效果,在循环冷却水新系统开车之前须先清洗后再进行预膜处理,而老系统在检修、酸洗后也要进行预膜处理。Pre-film is one of the essential and important links in industrial water treatment technology, and an important means to improve the corrosion resistance of circulating water equipment. Its purpose is to form a dense and corrosion-resistant protection layer on the metal surface after chemical cleaning. membrane. For the same circulating cooling water treatment formula, whether it is pre-coated or not directly affects the corrosion inhibition effect of the formula, and the corrosion rate is about 20 times worse. In order to improve the corrosion inhibition effect of the formula, the new circulating cooling water system must be cleaned before pre-coating treatment before starting up, and the old system must also be pre-coated after overhaul and pickling.
循环冷却水系统的预膜剂常常由缓蚀剂和适量的阻垢分散剂组成,循环冷却水处理缓蚀剂的使用始于20世纪20年代使用三聚磷酸钠,40年代开始发展,到目前为止经过了70多年的发展,经历了:铬酸盐(20世纪40~50年代)——聚磷酸盐(20世纪60年代)——有机膦酸盐(20世纪70年代)——低磷缓蚀剂有机膦羧酸(20世纪80年代)——非磷缓蚀剂(20世纪80年代)等几个使用阶段。铬酸盐虽然缓蚀效果良好,但由于本身的毒性,逐步被聚磷酸盐所代替。聚磷酸盐如三聚磷酸钠、六偏磷酸纳,是一类典型的阴极型缓蚀剂,在钙镁等二价金属离子浓度大于50mg/L的水质中,能与钙镁等两价金属离子作用形成沉积保护膜,缓蚀效果良好,但由于本身的结构不稳定,易水解出正磷酸根,导致磷酸盐垢形成;此外磷酸盐排入水体可造成环境富营养化污染。20世纪70年代,出现了有机膦酸类缓蚀剂,如羟基亚乙基二膦酸(HEDP)、胺基三亚甲基膦酸(ATMP)、乙二胺四亚甲基膦酸(EDTMP)、二亚乙基三胺五亚甲基膦酸(DETPMP)等,这些有机膦酸盐由于结构稳定和磷含量较聚磷酸盐低,减少了形成磷酸钙垢的危险及对环境富营养化污染的压力,因此得到了迅速的发展。由于环境保护限制磷的排放,20世纪80年代出现了含磷更低的有机膦羧酸缓蚀剂,如2-膦酸基-1,2,4-三羧酸(PBTCA)、2-羟基膦基乙酸(HPAA)。在这一时期非磷缓蚀剂如硅酸盐、钼酸盐、钨酸盐也开始试用,硅酸盐价廉无毒,但控制不好会形成难以清洗的硅垢;而钼酸盐和钨酸盐虽然无毒但由于价格高、使用剂量大,也限制了它们的推广。含磷缓蚀阻垢剂从聚磷酸盐、有机膦酸盐到有机膦羧酸,含磷量分别为六偏磷酸钠(Na6P6O18)为30.4%(以P计)、氨基三亚甲基膦酸(ATMP)为31.1%(以P计)、羟基亚亚乙基二膦酸(HEDP)为30.1%(以P计)、乙二胺四四亚甲基膦酸(EDTMP)为28.4%(以P计)、二亚乙基三胺五亚甲基膦酸(DEPTMP)为27.1%(以P计)、2-羟基膦基乙酸(HPA)为19.9%(以P计)、2-膦酸基-1,2,4-三羧酸(PBTCA)为11.9%(以P计),磷含量的逐渐减少体现了人类环境保护意识的提高。The pre-filming agent of the circulating cooling water system is often composed of corrosion inhibitors and appropriate scale inhibitors and dispersants. The use of corrosion inhibitors for circulating cooling water treatment began with the use of sodium tripolyphosphate in the 1920s, and began to develop in the 1940s. So far, after more than 70 years of development, it has experienced: chromate (1940s to 1950s) - polyphosphate (1960s) - organic phosphonate (1970s) - low phosphorus retardation Corrosion agent organic phosphine carboxylic acid (1980s) - non-phosphorus corrosion inhibitor (1980s) and other stages of use. Although chromate has good corrosion inhibition effect, it is gradually replaced by polyphosphate due to its toxicity. Polyphosphate, such as sodium tripolyphosphate and sodium hexametaphosphate, is a typical type of cathodic corrosion inhibitor. Ion action forms a deposition protective film, which has a good corrosion inhibition effect, but due to its unstable structure, orthophosphate is easily hydrolyzed, resulting in the formation of phosphate scale; in addition, phosphate discharge into water can cause environmental eutrophication pollution. In the 1970s, organic phosphonic acid corrosion inhibitors appeared, such as hydroxyethylene diphosphonic acid (HEDP), amino trimethylene phosphonic acid (ATMP), ethylenediamine tetramethylene phosphonic acid (EDTMP) , diethylenetriaminepentamethylenephosphonic acid (DETPMP), etc. These organic phosphonates have a stable structure and lower phosphorus content than polyphosphates, reducing the risk of calcium phosphate scale formation and environmental eutrophication pollution pressure, and thus developed rapidly. Due to environmental protection restrictions on phosphorus emissions, organic phosphonic acid corrosion inhibitors with lower phosphorus content appeared in the 1980s, such as 2-phosphonic acid-1,2,4-tricarboxylic acid (PBTCA), 2-hydroxy Phosphonoacetic acid (HPAA). During this period, non-phosphorus corrosion inhibitors such as silicate, molybdate, and tungstate also began to be tried. Silicate is cheap and non-toxic, but if it is not well controlled, it will form silicon scale that is difficult to clean; and molybdate and Although tungstates are non-toxic, their promotion is limited due to their high price and large dosage. Phosphorus-containing corrosion and scale inhibitors range from polyphosphate, organic phosphonate to organic phosphine carboxylic acid. Methylphosphonic acid (ATMP) is 31.1% (calculated as P), hydroxyethylene diphosphonic acid (HEDP) is 30.1% (calculated as P), ethylenediaminetetramethylenephosphonic acid (EDTMP) is 28.4% (calculated by P), 27.1% (calculated by P) of diethylenetriaminepentamethylenephosphonic acid (DEPTMP), 19.9% (calculated by P) of 2-hydroxyphosphinoacetic acid (HPA), 2-phosphono-1,2,4-tricarboxylic acid (PBTCA) is 11.9% (calculated as P), and the gradual reduction of phosphorus content reflects the improvement of human environmental protection awareness.
在循环水处理技术中,由于较早地使用了缓蚀剂,设备的腐蚀问题得到了一定的缓解,结垢问题就显得更加突出,迫使人们致力于解决结垢问题。循环冷却水处理阻垢分散剂的使用要比缓蚀剂晚,起步于20世纪60年代使用木质素磺酸纳,其发展经历了天然阻垢分散剂(20世纪60年代的起步阶段)——聚羧酸盐(20世纪70年代)——二元及三元羧酸共聚物——多官能团共聚物(20世纪80年代)——低磷新型有机高分子化合物(20世纪90年代)——无磷生物可降解聚合物(20世纪90年代末至21世纪初)。天然阻垢分散剂木质素磺酸钠、腐殖酸钠虽然环保、有一定的阻垢作用,能部分解决水垢沉积和锌盐稳定问题,但远远满足不了循环冷却水系统对阻垢性能的要求。聚合物阻垢分散剂的发展从聚羧酸类、二元及三元羧酸共聚物发展到含多官能团共聚物,使水处理技术取得了突破性进展,它们由于无磷,曾被认为是无毒、污染很小、环境可接受的水处理药剂,但却忽略了它们在环境中的长期累积而造成的潜在危害。因为近年来的研究表明:尽管多数羧酸类聚合物及共聚物虽然毒性较低,但它们一般无法在微生物和真菌的作用下分解成简单无毒的物质,即无法生物降解或只能少量被生物降解,若在水体中长期富集,也将污染环境,尤其是在一些对环保要求比较严格的领域如海上油田等。因此进入20世纪90年代,美国、日本、德国等几家知名的水处理企业都相继开始致力于寻找一种能替代聚羧酸,在具有优良的阻垢缓蚀性能的同时,又可被生物降解的“绿色环保”型水处理化学品。无磷、生物可降解绿色缓蚀阻垢剂聚天冬氨酸和聚氧琥珀酸的开发,表明绿色阻垢剂已成为水处理药剂发展的方向。In circulating water treatment technology, due to the early use of corrosion inhibitors, the corrosion problem of equipment has been alleviated to a certain extent, and the scaling problem has become more prominent, forcing people to devote themselves to solving the scaling problem. The use of scale inhibitors and dispersants for circulating cooling water treatment is later than that of corrosion inhibitors. It started to use sodium lignosulfonate in the 1960s, and its development has experienced natural scale inhibitors and dispersants (initial stage in the 1960s)—— Polycarboxylates (1970s) - binary and tricarboxylic acid copolymers - multifunctional copolymers (1980s) - low-phosphorus new organic polymers (1990s) - Phosphorus-free biodegradable polymers (late 1990s to early 2000s). Although natural scale inhibitors such as sodium lignosulfonate and sodium humate are environmentally friendly and have a certain scale inhibition effect, they can partially solve the problems of scale deposition and zinc salt stability, but they are far from meeting the scale inhibition performance of the circulating cooling water system. Require. The development of polymer scale inhibitors and dispersants has developed from polycarboxylic acids, dibasic and tribasic carboxylic acid copolymers to multifunctional copolymers, which has made breakthroughs in water treatment technology. Because they are phosphorus-free, they were once considered to be Non-toxic, less polluting and environmentally acceptable water treatment chemicals, but the potential harm caused by their long-term accumulation in the environment is ignored. Because studies in recent years have shown that although most carboxylic acid polymers and copolymers have low toxicity, they generally cannot be decomposed into simple non-toxic substances under the action of microorganisms and fungi, that is, they cannot be biodegraded or can only be destroyed in a small amount. Biodegradation, if enriched in water for a long time, will also pollute the environment, especially in some areas with strict environmental protection requirements such as offshore oil fields. Therefore, in the 1990s, several well-known water treatment companies in the United States, Japan, Germany, etc. began to work on finding an alternative to polycarboxylic acid, which has excellent scale and corrosion inhibition properties and can be biologically Degradable "green" water treatment chemicals. The development of phosphorus-free, biodegradable green corrosion and scale inhibitors polyaspartic acid and polyoxysuccinic acid indicates that green scale inhibitors have become the development direction of water treatment chemicals.
现有的预膜技术中,常常采用传统预膜剂,即磷锌预膜剂,它是一种以聚磷酸盐和锌盐为主要成分的固体预膜剂,通常由65%~70%的六偏磷酸钠和30%~35%的七水硫酸锌混合而成,使用浓度为200~250mg·L-1,pH需控制在5.5~6.5。该预膜剂在运行时由于聚磷酸盐易于水解,易形成磷酸钙沉淀,通常在预膜24h后,要加入30~100mg·L-1的聚合物分散剂(通常是聚羧酸盐类或聚羧酸盐类共聚物)来防止磷酸钙垢和锌盐的沉积。这种预膜剂效果虽好,但存在着诸多弊端:(1)聚磷酸盐在水中极易分解,形成磷酸钙沉淀;(2)药剂易吸潮结块,现场加药极为不便,且药剂加到系统中常常有许多不溶物,水的浊度较高(>20mg·L-1);(3)预膜条件(温度、pH)较为苛刻,预膜时需要加入大量的氨基磺酸或硫酸调节pH;(4)预膜剂的用量较大,预膜效果不稳定;(5)预膜结束后,要采取大排(排出预膜液)大补(补充新鲜水)的方式才能转换至正常运行,置换时间较长,水的耗量相对较多;(6)高磷配方,磷作为营养源,使水体富营养化,破坏生态平衡;(7)运行管理繁琐。因此寻求一种不调pH、预膜效果好、运行管理方便、预膜后不需置换即可直接转入正常运行、无污染的新型环保预膜剂是解决循环冷却水系统是解决上述传统预膜剂弊端的一条有效途径。In the existing pre-film technology, the traditional pre-film agent is often used, that is, the phosphorus-zinc pre-film agent. It is a solid pre-film agent with polyphosphate and zinc salt as the main components. It usually consists of 65% to 70% Sodium hexametaphosphate is mixed with 30% to 35% zinc sulfate heptahydrate, the concentration used is 200 to 250 mg·L -1 , and the pH needs to be controlled at 5.5 to 6.5. The pre-filming agent is easy to hydrolyze and form calcium phosphate precipitation during operation. Usually, after 24 hours of pre-filming, 30-100 mg·L -1 polymer dispersant (usually polycarboxylate or Polycarboxylate copolymer) to prevent the deposition of calcium phosphate scale and zinc salts. Although the effect of this pre-film agent is good, there are many disadvantages: (1) polyphosphate is very easy to decompose in water, forming calcium phosphate precipitation; There are often many insoluble substances added to the system, and the turbidity of the water is relatively high (>20mg·L -1 ); (3) The pre-film conditions (temperature, pH) are relatively harsh, and a large amount of sulfamic acid or Sulfuric acid adjusts the pH; (4) the amount of pre-film agent is large, and the pre-film effect is unstable; (5) after the pre-film is completed, it is necessary to adopt a large discharge (discharge of the pre-film liquid) and a large supplement (supplement of fresh water) to convert To normal operation, the replacement time is long, and the water consumption is relatively large; (6) high-phosphorus formula, phosphorus is used as a nutrient source, which makes the water body eutrophic and destroys the ecological balance; (7) operation and management are cumbersome. Therefore, seeking a new environmentally friendly pre-film agent that does not adjust the pH, has a good pre-film effect, is convenient for operation and management, can be directly transferred to normal operation without replacement after pre-film, and is pollution-free is the solution to the problem of the traditional pre-film solution for the circulating cooling water system. An effective approach to the drawbacks of film agents.
中国专利申请公开号CN1715447A公开了一种循环冷却水系统预膜剂,由重量百分比分别为40~60%的六偏磷酸钠、10~15%的硫酸锌、5~11%的三聚磷酸钠、4~8%的氨基三甲叉膦酸、3~6%的丙烯酸-丙烯酸酯共聚物、余量的水组成。该配方与传统预膜剂相比,除了聚磷酸盐、硫酸锌外添加了有机膦酸盐(氨基三甲叉膦酸)、羧酸共聚物(丙烯酸-丙烯酸酯共聚物),提高了预膜剂的使用效果,同时对预膜的条件要求也较宽松。但该配方仍然是高磷配方,且预膜后仍然需要置换水质转入正常运行。由于置换出的预膜排污水含有较高的磷,排入水体中会对环境造成污染。Chinese Patent Application Publication No. CN1715447A discloses a pre-film agent for circulating cooling water system, which consists of 40-60% sodium hexametaphosphate, 10-15% zinc sulfate, and 5-11% sodium tripolyphosphate. , 4-8% of aminotrimethylene phosphonic acid, 3-6% of acrylic acid-acrylic acid ester copolymer, and the rest of water. Compared with the traditional pre-filming agent, this formula adds organic phosphonate (aminotrimethylene phosphonic acid) and carboxylic acid copolymer (acrylic acid-acrylate copolymer) in addition to polyphosphate and zinc sulfate, which improves the pre-filming agent. The use effect of the film is also relatively loose. However, the formula is still a high-phosphorus formula, and after pre-filming, it still needs to replace the water quality and turn it into normal operation. Since the replaced pre-membrane sewage contains high phosphorus, it will pollute the environment if it is discharged into the water body.
中国专利ZL02158580.6提供了一种不调pH的循环冷却水系统预膜剂,由重量百分比分别为2~10%的磷酸、1~10%的磷酸二氢锌、5~18%的有机膦酸、4.5~10.5%的含羧酸基共聚物、0.5~2.0%的苯并三氮唑和余量的水组成。与传统预膜剂相比,该配方用有机膦酸代替了部分无机磷酸,使含磷量有所降低;且使用时不需调pH、加药方便、浊度小,但该配方仍含有较高的磷,且预膜结束后仍需置换水质转入正常运行。由于置换出的预膜排污水含有较高的磷,排入水体中仍然会对环境造成污染。Chinese patent ZL02158580.6 provides a pre-coating agent for circulating cooling water systems without pH adjustment, which consists of 2-10% phosphoric acid, 1-10% zinc dihydrogen phosphate, and 5-18% organic phosphine Acid, 4.5-10.5% of copolymer containing carboxylic acid groups, 0.5-2.0% of benzotriazole and the rest of water. Compared with the traditional pre-filming agent, this formula uses organic phosphonic acid instead of part of inorganic phosphoric acid, which reduces the phosphorus content; and it does not need to adjust pH when using, it is convenient to add medicine, and the turbidity is small, but the formula still contains relatively High phosphorus, and after the pre-membrane is completed, the water quality still needs to be replaced to return to normal operation. Since the replaced pre-film sewage contains high phosphorus, it will still pollute the environment if it is discharged into the water body.
为了达到环保的目的,本发明采用含磷量最低的有机膦缓蚀剂2-膦酸基-1,2,4-三羧酸(PBTCA)和无磷、可生物降解的聚环氧琥珀酸(PESA)作为预膜剂的主要成分,PESA不仅具有阻垢分散作用,而且能在碳钢表面形成防腐保护膜。目前以2-膦酸基-1,2,4-三羧酸(PBTCA)和聚环氧琥珀酸(PESA)为主要成分的预膜剂还没未见报道。In order to achieve the purpose of environmental protection, the present invention adopts organic phosphine corrosion inhibitor 2-phosphonic acid group-1,2,4-tricarboxylic acid (PBTCA) with the lowest phosphorus content and phosphorus-free, biodegradable polyepoxysuccinic acid (PESA) As the main component of the pre-film agent, PESA not only has the function of scale inhibition and dispersion, but also can form an anti-corrosion protective film on the surface of carbon steel. At present, there is no report on the pre-film agent mainly composed of 2-phosphono-1,2,4-tricarboxylic acid (PBTCA) and polyepoxysuccinic acid (PESA).
发明内容Contents of the invention
本发明的目的之一在于提供一种低磷用于处理循环冷却水预膜处理的环保型复合预膜剂,以克服现有的预膜剂配方含磷较高、易引起水体的富营养化的问题。One of the objectives of the present invention is to provide a low-phosphorus environmental-friendly composite pre-film agent for pre-film treatment of circulating cooling water, so as to overcome the high phosphorus content of the existing pre-film agent formula and easily cause eutrophication of water bodies The problem.
本发明的目的之二在于提供一种环保型复合预膜剂的使用方法。使用本环保型复合预膜剂后不用置换水质、可直接转入正常运行的预膜处理配方,克服了现有的预膜剂配方在预膜结束后需置换水质才能转入正常运行,不仅节约了大量的置换水,而且由于没有预膜废液的排放,减少了对环境的污染。The second object of the present invention is to provide a method for using an environment-friendly composite pre-film agent. After using this environment-friendly composite pre-film agent, there is no need to replace the water quality, and the pre-film treatment formula can be directly transferred to normal operation. A large amount of water is replaced, and because there is no discharge of pre-membrane waste liquid, the pollution to the environment is reduced.
为实现上述目的,本发明提出的低磷环保型复合预膜剂,该复合预膜剂由2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、聚环氧琥珀酸钠为主要成分(PESA),并添加适量的羧酸基共聚物、钼酸钠(Na2MoO4)、苯并三氮唑、硫酸锌(ZnSO4)及水组成,其组分的重量百分比如下:In order to achieve the above object, the low-phosphorous environment-friendly composite pre-film agent proposed by the present invention, the composite pre-film agent consists of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA), polyepoxysuccinic acid Sodium is the main component (PESA), and an appropriate amount of carboxylic acid-based copolymer, sodium molybdate (Na 2 MoO 4 ), benzotriazole, zinc sulfate (ZnSO 4 ) and water are added, and the weight percentage of its components as follows:
PBTCA 12%~18%PBTCA 12%~18%
PESA 6%~15%PESA 6%~15%
羧酸基共聚物 0.3%~2%Carboxylic acid-based copolymer 0.3%~2%
苯骈三氮唑 0.5%~2%Benzotriazole 0.5%~2%
Na2MoO4 0.5%~2% Na2MoO4 0.5 %~2%
ZnSO4 2%~5% ZnSO4 2%~5%
其余为水,其总重量满足100%。The rest is water, and its total weight satisfies 100%.
本发明中,所述2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)为市售的液体制剂,有效浓度为50%。In the present invention, the 2-phosphono-1,2,4-tricarboxylic butane (PBTCA) is a commercially available liquid preparation with an effective concentration of 50%.
本发明中,所述聚环氧琥珀酸钠为市售的液体制剂,固含量为40%,其结构式为:In the present invention, the sodium polyepoxysuccinate is a commercially available liquid preparation with a solid content of 40%, and its structural formula is:
其中,聚合度n为整数,范围4~50,较佳聚合度范围4~25。Wherein, the degree of polymerization n is an integer in the range of 4-50, preferably in the range of 4-25.
本发明中,所述的羧酸基共聚物为丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)或丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸/丙烯酸羟丙酯三元共聚物(AA/AMPS/HPA),是市售的液体制剂,其固含量为30%。In the present invention, the carboxylic acid-based copolymer is acrylic acid/2-methyl-2'-acrylamido propane sulfonic acid binary copolymer (AA/AMPS) or acrylic acid/2-methyl-2'- Acrylamidopropanesulfonic acid/hydroxypropyl acrylate terpolymer (AA/AMPS/HPA), is a commercially available liquid formulation with a solids content of 30%.
本发明中,所述苯并三氮唑为市售的固体制剂。In the present invention, the benzotriazole is a commercially available solid preparation.
本发明中,所述钼酸钠为市售的固体制剂二水钼酸钠(Na2MoO4·2H2O)。In the present invention, the sodium molybdate is a commercially available solid preparation sodium molybdate dihydrate (Na 2 MoO 4 ·2H 2 O).
本发明中,所述硫酸锌为市售的七水硫酸锌(ZnSO4·7H2O)。In the present invention, the zinc sulfate is commercially available zinc sulfate heptahydrate (ZnSO 4 ·7H 2 O).
本发明中的复合预膜剂是由PBTCA、聚环氧琥珀酸钠、羧酸基共聚物、苯并三氮唑、钼酸钠、硫酸锌等六种成分组成。由于这六种成分中的PBTCA及羧酸基共聚物是酸性产品,聚环氧琥珀酸钠、钼酸钠为碱性的钠盐,且聚环氧琥珀酸在酸性条件下由于溶解度大大降低,在高浓度时会产生沉积;而咪唑啉型缓蚀剂则在酸性环境中溶解度极低(<1%),甚至不溶,而在碱性环境中溶于水;锌盐溶于酸性水溶剂中,但在碱性环境中将会沉积。因此,本发明的复合预膜剂的制备方法如下:将PBTCA、羧酸基共聚物与水混合并搅拌均匀,然后加入七水硫酸锌搅拌溶解,即得A剂,备用;将聚环氧琥珀酸钠与水混合并搅拌均匀,然后加入苯并三氮唑、钼酸钠搅拌溶解,即得B剂,备用。The composite pre-film agent in the present invention is composed of six components such as PBTCA, sodium polyepoxysuccinate, carboxylic acid-based copolymer, benzotriazole, sodium molybdate, and zinc sulfate. Because PBTCA and carboxylic acid-based copolymers in these six components are acidic products, sodium polyepoxysuccinate and sodium molybdate are alkaline sodium salts, and polyepoxysuccinic acid is greatly reduced due to solubility under acidic conditions. Deposits will occur at high concentrations; imidazoline corrosion inhibitors have very low solubility (<1%) or even insoluble in acidic environments, but are soluble in water in alkaline environments; zinc salts are soluble in acidic water solvents , but will be deposited in an alkaline environment. Therefore, the preparation method of the composite prefilming agent of the present invention is as follows: mix PBTCA, carboxylic acid-based copolymer with water and stir evenly, then add zinc sulfate heptahydrate and stir to dissolve, to obtain agent A, for subsequent use; Mix sodium molybdate with water and stir evenly, then add benzotriazole and sodium molybdate, stir and dissolve, and obtain agent B for later use.
本发明所述的环保型复合预膜剂在使用时,投加时只要将A剂及B剂直接加入循环冷却水中即可,加入量为300~400mg/L。When the environment-friendly composite pre-film agent of the present invention is used, it is only necessary to directly add agent A and agent B into the circulating cooling water when adding, and the addition amount is 300-400mg/L.
本发明经过实验研究发现:当单独使用PBTCA时,在50~100mg/L的浓度范围时,即可在碳钢试片表面成膜,用硫酸铜标准点滴液检验,所成膜的耐蚀性为15~25s。而单独使用PESA时,在50~100mg/L的浓度范围时,也可在碳钢试片表面成膜,用硫酸铜标准点滴液检验,所成膜的耐蚀性为11~20s。The present invention finds through experimental research that when PBTCA is used alone, a film can be formed on the surface of the carbon steel test piece in the concentration range of 50-100 mg/L, and the corrosion resistance of the formed film can be tested by copper sulfate standard drop solution. 15-25s. When PESA is used alone, it can also form a film on the surface of a carbon steel test piece at a concentration range of 50-100mg/L, and the corrosion resistance of the formed film is 11-20s when tested by copper sulfate standard drop solution.
本发明经研究发现:当PBTCA与PESA配合使用进行预膜时,存在着良好的协同效应,比各自单独使用时的预膜效果要好,当两者的总浓度50~100mg/L,所成膜的耐蚀性为25~35s。The present invention finds through research: when PBTCA and PESA are used together for pre-filming, there is a good synergistic effect, which is better than the effect of pre-filming when they are used alone. When the total concentration of the two is 50-100mg/L, the film formed The corrosion resistance is 25 ~ 35s.
本发明经研究还发现,当在PBTCA、PESA为主要成分的基础上加入适量的钼酸钠、锌盐、苯并三氮唑,可以大大提高成膜的耐蚀性,其膜的耐蚀性大于150s。但由PBTCA、PESA、钼酸钠、锌盐、苯并三氮唑这几种成分组成预膜剂虽然大大提高了预膜的耐蚀性,但预膜的水质稍微有点浑浊。The present invention also finds through research that when adding an appropriate amount of sodium molybdate, zinc salt, and benzotriazole on the basis of PBTCA and PESA as the main components, the corrosion resistance of the film can be greatly improved, and the corrosion resistance of the film can be greatly improved. greater than 150s. However, although the pre-film agent composed of PBTCA, PESA, sodium molybdate, zinc salt, and benzotriazole greatly improves the corrosion resistance of the pre-film, the water quality of the pre-film is slightly turbid.
本发明经过研究发现,在由PBTCA、PESA、钼酸钠、锌盐、苯并三氮唑这几种成分组成预膜剂中,加入少量的羧酸基共聚物,就可大大改善预膜液的水质使其保持澄清透明,保证了预膜后的预膜液不需置换就可直接转为正常运行。The present invention has found through research that, in the pre-film agent composed of several components such as PBTCA, PESA, sodium molybdate, zinc salt, and benzotriazole, adding a small amount of carboxylic acid-based copolymer can greatly improve the pre-film agent. The water quality keeps it clear and transparent, ensuring that the pre-film liquid after pre-film can be directly converted to normal operation without replacement.
本发明提供的环保型复合预膜剂与传统预膜剂相比具有如下优点:(1)本发明提供的复合预膜剂具有低磷的特点,使用过程中循环冷却水的总磷(P)含量<7.5mg·L-1,而传统预膜剂在使用时其总磷(P)含量在40mg·L-1~60mg·L-1;(2)本发明提供的复合预膜剂中,所用的聚合物聚环氧琥珀酸钠为生物可降解产品,属于无磷、生物可降解的环境友好产品;(3)本发明中的PBTCA、聚环氧琥珀酸、羧酸基共聚物、苯并三氮唑、钼酸盐、锌盐之间存在着明显的预膜协同效应,因而大大降低了总药剂使用浓度;(4)本发明提供的复合预膜剂在对碳钢进行预膜时,药剂总用量少,成膜快(48h),所成膜的耐蚀性好(>150s),远优于循环冷却水系统化学清洗和预膜工艺技术规程(CECS103:99)中规定的预膜技术指标(>10s);(5)本发明提供的复合预膜剂在对循环冷却水系统进行预膜时,不需调节加酸调节pH,因此不需专用的加酸设备,不仅节省了费用,而且简化了运行时的操作;(6)本发明提供的复合预膜剂在进行预膜时,预膜液不需置换和排放,即可直接转为正常运行,不仅节约了大量的置换水,而且节约了传统预膜结束后所需的就药剂基础投加费用,同时也减少了废水的排放,因此本发明不仅可以节约成本,而且可以减少废水排放;(7)该预膜配方转入正常运行后预膜剂本身可直接作为正常运行的缓蚀阻垢剂,随着系统正常运行的进行,原有的预膜剂通过循环冷却水的排污系统将逐渐降至正常运行的浓度之下,此时即可通过补充水投加以PESA、PBTCA为主要成分的缓蚀阻垢配方,也可通过补充水投加新的缓蚀阻垢配方代替原有的预膜剂,原有的预膜剂不影响新的缓蚀阻垢配方的投加。The environment-friendly composite pre-film agent provided by the invention has the following advantages compared with the traditional pre-film agent: (1) the composite pre-film agent provided by the invention has the characteristics of low phosphorus, and the total phosphorus (P) of circulating cooling water in the use process Content <7.5mg·L -1 , while the total phosphorus (P) content of the traditional prefilming agent in use is 40mg·L -1 ~ 60mg·L -1 ; (2) In the composite prefilming agent provided by the present invention, The polymer sodium polyepoxysuccinate used is a biodegradable product, which belongs to a phosphorus-free, biodegradable environment-friendly product; (3) PBTCA in the present invention, polyepoxysuccinic acid, carboxylic acid-based copolymer, benzene There is an obvious pre-film synergistic effect between triazole, molybdate, and zinc salt, thereby greatly reducing the total agent concentration; (4) the composite pre-film agent provided by the invention is used when carbon steel is pre-filmed , the total dosage of chemicals is small, the film formation is fast (48h), and the corrosion resistance of the formed film is good (>150s), which is far superior to that stipulated in the technical regulations for chemical cleaning and pre-filming of circulating cooling water systems (CECS103:99) Pre-film technical index (>10s); (5) when the composite pre-film agent provided by the present invention performs pre-film on the circulating cooling water system, it is not necessary to adjust the pH by adding acid, so no special acid-adding equipment is needed, which not only saves (6) when the composite pre-film agent provided by the present invention performs pre-film, the pre-film liquid can be directly converted to normal operation without replacement and discharge, which not only saves a large amount of Replace the water, and save the cost of adding basic medicament after the traditional pre-film is finished, and also reduce the discharge of waste water, so the present invention can not only save costs, but also reduce waste water discharge; (7) the pre-film formula After being transferred to normal operation, the pre-film agent itself can be directly used as a corrosion and scale inhibitor in normal operation. With the normal operation of the system, the original pre-film agent will gradually reduce to the concentration of normal operation through the sewage system of circulating cooling water At this time, the corrosion and scale inhibition formula with PESA and PBTCA as the main components can be added through supplementary water, or a new corrosion and scale inhibition formula can be added through supplementary water to replace the original pre-film agent. The pre-film agent does not affect the addition of new corrosion and scale inhibition formula.
具体实施方式Detailed ways
下面通过实施例进一步描述本发明,但不局限于其范围。The present invention is further described below by way of examples, but not limiting its scope.
下面的实施例均参照《水处理剂缓蚀性能的测定-旋转挂片法》(中华人民共和国国家标准GB/T18175-2000)进行旋转挂片预膜实验。实验采用RCC-II型旋转挂片腐蚀测试仪,温度45℃,转速75r/min,预膜实验时间48小时,碳钢试片为A3碳钢,实验用水为某钢铁厂循环冷却水补充水,其水质指标为:Ca2+(以CaCO3计)150~250mg·L-1,总碱度(以CaCO3计)80~260mg·L-1,Cl- 50~100mg·L-1,SO4 2-50~150mg·L-1,pH7.4~8.4。The following examples all refer to "Measurement of Corrosion Inhibition Performance of Water Treatment Agents-Rotary Coupon Method" (National Standard of the People's Republic of China GB/T18175-2000) to carry out the rotary coupon pre-coating experiment. The experiment adopts the RCC-II rotary coupon corrosion tester, the temperature is 45°C, the rotation speed is 75r/min, the pre-film test time is 48 hours, the carbon steel test piece is A 3 carbon steel, and the test water is the circulating cooling water replenishment water of a steel plant , its water quality indicators are: Ca 2+ (calculated as CaCO 3 ) 150-250 mg·L -1 , total alkalinity (calculated as CaCO 3 ) 80-260 mg·L -1 , Cl - 50-100 mg·L -1 , SO 4 2- 50~150 mg·L -1 , pH 7.4~8.4.
预膜结束后取出试片,先用蒸馏水冲洗表面,再用无水乙醇擦拭,然后用电吹风吹干。观察膜表面的特征,用硫酸铜标准点滴液检验膜的耐蚀时间,通过比较预膜试片与空白试片点滴时出现红点的时间差来评价膜的优劣。硫酸铜标准点滴液的制备:称取5g硫酸铜和15g氯化钠溶解于100ml蒸馏水中即可。After the pre-filming, take out the test piece, first rinse the surface with distilled water, then wipe it with absolute ethanol, and then dry it with a hair dryer. Observe the characteristics of the film surface, test the corrosion resistance time of the film with copper sulfate standard drip solution, and evaluate the quality of the film by comparing the time difference between the pre-film test piece and the blank test piece when the red dot appears. Preparation of copper sulfate standard drop solution: weigh 5g of copper sulfate and 15g of sodium chloride and dissolve in 100ml of distilled water.
实施例1Example 1
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将65.00g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、4.80g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、19.20g的水混合搅拌均匀,再加入11.00g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of agent A: 65.00g of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA) with a solid content of 50% and 4.80g of acrylic acid/2-methyl-butane with a solid content of 30% Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 19.20 g of water evenly, then add 11.00 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the required A agent.
B剂的配制:将31.2g固含量为40%的聚环氧琥珀酸钠与63.3g水混合并搅拌均匀,再加入2.5g的苯并三氮唑及3.0g二水钼酸钠(Na2MoO4·2H2O)搅拌溶解,即得到所需配制的100gB剂。Preparation of agent B: 31.2g solid content is 40% sodium polyepoxysuccinate mixed with 63.3g water and stirred evenly, then add 2.5g benzotriazole and 3.0g sodium molybdate dihydrate ( Na MoO 4 ·2H 2 O) was stirred and dissolved to obtain 100 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加200mg·L-1,B剂投加200mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)150mg·L-1、总碱度(以CaCO3计)126mg·L-1、Cl- 67mg·L-1、SO4 2-67mg·L-1、pH7.4。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the test water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, add 200mg·L -1 to agent A, and add 200mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 150mg·L -1 , total alkalinity (calculated as CaCO 3 ) 126mg·L -1 , Cl - 67mg·L -1 , SO 4 2- 67mg·L -1 , pH 7.4. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量400mg·L-1(A剂200mg·L-1,B剂200mg·L-1)为基础计算,各组分的重量百分比如下:Based on the dosage of 400mg·L -1 of a pre-film agent (200mg·L -1 of A agent and 200mg·L -1 of B agent), the weight percentage of each component is as follows:
PBTCA 16.25%PBTCA 16.25%
PESA 6.24%PESA 6.24%
AA/AMPS 0.72%AA/AMPS 0.72%
苯并三氮唑 1.25%Benzotriazole 1.25%
Na2MoO4 1.28%Na 2 MoO 4 1.28%
ZnSO4 3.09% ZnSO4 3.09%
水 71.17%。Water 71.17%.
实施例2Example 2
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将66.60g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、2.70g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、18.70g的水混合搅拌均匀,再加入12.00g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of Agent A: 66.60g solid content of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA), 2.70g solid content of 30% acrylic acid/2-methyl- Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 18.70 g of water evenly, then add 12.00 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the required A agent.
B剂的配制:将50.00g固含量为40%的聚环氧琥珀酸钠与16.0g水混合并搅拌均匀,再加入2.00g的苯并三氮唑及4.00g二水钼酸钠(Na2MoO4·2H2O)搅拌溶解,即得到所需配制的100gB剂。Preparation of agent B: 50.00g solid content is 40% sodium polyepoxysuccinate mixed with 16.0g water and stirred evenly, then add 2.00g benzotriazole and 4.00g sodium molybdate dihydrate (Na 2 MoO 4 ·2H 2 O) was stirred and dissolved to obtain 100 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加150mg·L-1,B剂投加150mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)155mg·L-1、总碱度(以CaCO3计)160mg·L-1、Cl- 65mg·L-1、SO4 2-56mg·L-1、pH7.6。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the test water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, add 150mg·L -1 to agent A, and add 150mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 155mg·L -1 , total alkalinity (calculated as CaCO 3 ) 160mg·L -1 , Cl - 65mg·L -1 , SO 4 2- 56mg·L -1 , pH 7.6. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量300mg·L-1(A剂150mg·L-1,B剂150mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of 300mg·L -1 of a pre-film agent (150mg·L -1 for A agent and 150mg·L -1 for B agent), the weight percentage is as follows:
PBTCA 16.65%PBTCA 16.65%
PESA 10.00%PESA 10.00%
AA/AMPS 0.41%AA/AMPS 0.41%
苯并三氮唑 1.00%Benzotriazole 1.00%
Na2MoO4 1.70%Na 2 MoO 4 1.70%
ZnSO4 3.37% ZnSO4 3.37%
水 66.87%。Water 66.87%.
实施例3Example 3
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将60.00g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、3.60g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、19.60g的水混合搅拌均匀,再加入16.80g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of agent A: 60.00g of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA) with a solid content of 50% and 3.60g of acrylic acid/2-methyl-butane with a solid content of 30% Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 19.60 g of water evenly, then add 16.80 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the required A agent.
B剂的配制:将31.20g固含量为40%的聚环氧琥珀酸钠与64.50g水混合并搅拌均匀,再加入2.00g的苯并三氮唑及2.30g的二水钼酸钠(Na2MoO4·2H2O)搅拌溶解,即得到所需配制的100.00gB剂。The preparation of agent B: 31.20g solid content is 40% sodium polyepoxysuccinate and 64.50g water mix and stir, then add 2.00g of benzotriazole and 2.30g of sodium molybdate dihydrate (Na 2 MoO 4 ·2H 2 O) was stirred and dissolved to obtain 100.00 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加200mg·L-1,B剂投加200mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)230mg·L-1、总碱度(以CaCO3计)240mg·L-1、Cl- 76mg·L-1、SO4 2-88mg·L-1、pH8.0。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the test water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, add 200mg·L -1 to agent A, and add 200mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 230mg·L -1 , total alkalinity (calculated as CaCO 3 ) 240mg·L -1 , Cl - 76mg·L -1 , SO 4 2- 88mg·L -1 , pH 8.0. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量400mg·L-1(A剂200mg·L-1,B剂200mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of a pre-film agent of 400mg·L -1 (a dose of 200mg·L -1 , B dose of 200mg·L -1 ), the weight percentage is as follows:
PBTCA 15.00%PBTCA 15.00%
PESA 6.24%PESA 6.24%
AA/AMPS 0.54%AA/AMPS 0.54%
苯并三氮唑 1.00%Benzotriazole 1.00%
Na2MoO4 0.98%Na 2 MoO 4 0.98%
ZnSO4 4.71% ZnSO4 4.71%
水 71.53%。Water 71.53%.
实施例4Example 4
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将50.00g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、4.70g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、32.00g的水混合搅拌均匀,再加入13.30g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of agent A: 50.00g of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA) with a solid content of 50% and 4.70g of acrylic acid/2-methyl-butane with a solid content of 30% Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 32.00 g of water evenly, then add 13.30 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of A agent to be prepared.
B剂的配制:将43.80g固含量为40%的聚环氧琥珀酸钠与51.00g水混合并搅拌均匀,再加入1.50g的苯并三氮唑及3.70g的二水钼酸钠(Na2MoO4·2H2O)搅拌溶解,即得到所需配制的100.00gB剂。The preparation of agent B: 43.80g solid content is 40% sodium polyepoxysuccinate and 51.00g water are mixed and stirred evenly, then add 1.50g of benzotriazole and 3.70g of sodium molybdate dihydrate (Na 2 MoO 4 ·2H 2 O) was stirred and dissolved to obtain 100.00 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加200L-1,B剂投加200mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)210mg·L-1、总碱度(以CaCO3计)220mg·L-1、Cl- 80mg·L-1、SO4 2-108mg·L-1、pH8.1。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the test water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, add 200L -1 agent A, add 200mg·L agent B -1 , the experiment temperature is 45°C, the experiment time is 48h, the water quality of the experiment is: Ca 2+ (calculated as CaCO 3 ) 210mg·L -1 , total alkalinity (calculated as CaCO 3 ) 220mg·L -1 , Cl - 80mg ·L -1 , SO 4 2- 108 mg·L -1 , pH 8.1. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量400mg·L-1(A剂200mg·L-1,B剂200mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of a pre-film agent of 400mg·L -1 (a dose of 200mg·L -1 , B dose of 200mg·L -1 ), the weight percentage is as follows:
PBTCA 12.50%PBTCA 12.50%
PESA 8.7%PESA 8.7%
AA/AMPS 0.71%AA/AMPS 0.71%
苯并三氮唑 0.75%Benzotriazole 0.75%
Na2MoO4 1.58%Na 2 MoO 4 1.58%
ZnSO4 3.73% ZnSO4 3.73%
水 71.97%。Water 71.97%.
实施例5Example 5
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将68.60g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、9.60g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、11.70g的水混合搅拌均匀,再加入10.10g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of Agent A: 68.60g solid content of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA), 9.60g solid content of 30% acrylic acid/2-methyl- Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 11.70 g of water evenly, then add 10.10 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the required A agent.
B剂的配制:将42.90g固含量为40%的聚环氧琥珀酸钠与53.00g水混合并搅拌均匀,再加入2.30g的苯并三氮唑及1.80g的二水钼酸钠(Na2MoO4·2H2O)搅拌溶解,即得到所需配制的100.00gB剂。The preparation of agent B: 42.90g solid content is 40% sodium polyepoxysuccinate and 53.00g water mix and stir, then add 2.30g of benzotriazole and 1.80g of sodium molybdate dihydrate (Na 2 MoO 4 ·2H 2 O) was stirred and dissolved to obtain 100.00 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加175mg·L-1,B剂投加175mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)130mg·L-1、总碱度(以CaCO3计)126mg·L-1、Cl- 56mg·L-1、SO4 2-80mg·L-1、pH7.7。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the experimental water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, and add 175mg·L -1 to agent A and 175mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 130mg·L -1 , total alkalinity (calculated as CaCO 3 ) 126mg·L - 1, Cl - 56mg·L -1 , SO 4 2- 80mg·L -1 , pH 7.7. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量350mg·L-1(A剂175mg·L-1,B剂175mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of 350mg·L -1 of a pre-filming agent (175mg·L -1 of A agent and 175mg·L -1 of B agent), the weight percentage is as follows:
PBTCA 17.15%PBTCA 17.15%
PESA 8.58%PESA 8.58%
AA/AMPS 1.44%AA/AMPS 1.44%
苯并三氮唑 1.15%Benzotriazole 1.15%
Na2MoO4 0.77%Na 2 MoO 4 0.77%
ZnSO4 2.84% ZnSO4 2.84%
水 68.07%。Water 68.07%.
实施例6Example 6
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将57.20g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、4.00g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、28.80g的水混合搅拌均匀,再加入10.00g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of agent A: 57.20g solid content of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA), 4.00g solid content of 30% acrylic acid/2-methyl- Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 28.80 g of water evenly, then add 10.00 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the A agent to be prepared.
B剂的配制:将57.00g固含量为40%的聚环氧琥珀酸钠与39.20g水混合并搅拌均匀,再加入2.20g的苯并三氮唑及1.60g的二水钼酸钠(Na2MoO3·2H2O)搅拌溶解,即得到所需配制的100.00gB剂。The preparation of agent B: 57.00g solid content is 40% sodium polyepoxysuccinate and 39.20g water are mixed and stirred evenly, then add 2.20g of benzotriazole and 1.60g of sodium molybdate dihydrate (Na 2 MoO 3 .2H 2 O) was stirred and dissolved to obtain 100.00 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加175mg·L-1,B剂投加175mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)185mg·L-1、总碱度(以CaCO3计)166mg·L-1、Cl- 79mg·L-1、SO4 2-81mg·L-1、pH8.2。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the experimental water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, and add 175mg·L -1 to agent A and 175mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 185mg·L -1 , total alkalinity (calculated as CaCO 3 ) 166mg·L -1 , Cl - 79 mg·L -1 , SO 4 2- 81 mg·L -1 , pH 8.2. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量350mg·L-1(A剂175mg·L-1,B剂175mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of 350mg·L -1 of a pre-filming agent (175mg·L -1 of A agent and 175mg·L -1 of B agent), the weight percentage is as follows:
PBTCA 14.30%PBTCA 14.30%
PESA 11.40%PESA 11.40%
AA/AMPS 0.60%AA/AMPS 0.60%
苯并三氮唑 1.10%Benzotriazole 1.10%
Na2MoO4 0.68%Na 2 MoO 4 0.68%
ZnSO4 2.81% ZnSO4 2.81%
水 69.11%。Water 69.11%.
实施例7Example 7
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将51.60g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、2.80g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、35.60g的水混合搅拌均匀,再加入10.00g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of agent A: 51.60g solid content of 2-phosphonic acid group-1,2,4-tricarboxylic acid butane (PBTCA), 2.80g solid content of 30% acrylic acid/2-methyl- Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 35.60 g of water evenly, then add 10.00 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the required A agent.
B剂的配制:将64.5g固含量为40%的聚环氧琥珀酸钠与30.1g水混合并搅拌均匀,再加入2.8g的苯并三氮唑及2.6g的二水钼酸钠(Na2MoO3·2H2O)搅拌溶解,即得到所需配制的100gB剂。The preparation of agent B: 64.5g solid content is 40% sodium polyepoxysuccinate and 30.1g water mix and stir, then add 2.8g of benzotriazole and 2.6g of sodium molybdate dihydrate (Na 2 MoO 3 ·2H 2 O) stirring and dissolving to obtain 100g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加175mg·L-1,B剂投加175mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)150mg·L-1、总碱度(以CaCO3计)144mg·L-1、Cl- 101mg·L-1、SO4 2-58mg·L-1、pH8.0。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the experimental water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, and add 175mg·L -1 to agent A and 175mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 150mg·L -1 , total alkalinity (calculated as CaCO 3 ) 144mg·L -1 , Cl - 101 mg·L -1 , SO 4 2- 58 mg·L -1 , pH 8.0. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以按一种预膜剂的投加量350mg·L-1(A剂175mg·L-1,B剂175mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of 350mg·L -1 for one pre-film agent (175mg·L -1 for A dose and 175mg·L -1 for B dose), the weight percentage is as follows:
PBTCA 12.90%PBTCA 12.90%
PESA 12.90%PESA 12.90%
AA/AMPS 0.42%AA/AMPS 0.42%
苯并三氮唑 1.4%Benzotriazole 1.4%
Na2MoO4 1.11%Na 2 MoO 4 1.11%
ZnSO4 2.81% ZnSO4 2.81%
水 68.46%。Water 68.46%.
实施例8Example 8
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将50.00g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、5.00g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸二元共聚物(AA/AMPS)、36.10g的水混合搅拌均匀,再加入8.90g七水硫酸锌搅拌溶解,即得到所需配制的100.00gA剂。Preparation of Agent A: 50.00g of 2-phosphonic acid group-1,2,4-tricarboxylic butane (PBTCA) with a solid content of 50%, 5.00g of acrylic acid/2-methyl-butane with a solid content of 30% Mix and stir 2'-acrylamidopropanesulfonic acid binary copolymer (AA/AMPS) and 36.10 g of water evenly, then add 8.90 g of zinc sulfate heptahydrate and stir to dissolve, and obtain 100.00 g of the required A agent.
B剂的配制:将56.30g固含量为40%的聚环氧琥珀酸钠与38.40g水混合并搅拌均匀,再加入1.50g的苯并三氮唑及3.80g的二水钼酸钠(Na2MoO3·2H2O)搅拌溶解,即得到所需配制的100.00gB剂。The preparation of agent B: 56.30g solid content is 40% sodium polyepoxysuccinate and 38.40g water mix and stir, then add 1.50g of benzotriazole and 3.80g of sodium molybdate dihydrate (Na 2 MoO 3 .2H 2 O) was stirred and dissolved to obtain 100.00 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加200mg·L-1,B剂投加200mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)110mg·L-1、总碱度(以CaCO3计)132mg·L-1、Cl-96mg·L-1、SO4 2-81mg·L-1、pH7.8。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the test water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, add 200mg·L -1 to agent A, and add 200mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 110mg·L -1 , total alkalinity (calculated as CaCO 3 ) 132mg·L -1 , Cl - 96 mg·L -1 , SO 4 2- 81 mg·L -1 , pH 7.8. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以按一种预膜剂的投加量400mg·L-1(A剂200mg·L-1,B剂200mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of 400mg·L -1 for one pre-filming agent (200mg·L -1 for A agent, 200mg·L -1 for B agent), the weight percentage is as follows:
PBTCA 12.50%PBTCA 12.50%
PESA 11.26%PESA 11.26%
AA/AMPS 0.75%AA/AMPS 0.75%
苯并三氮唑 0.75%Benzotriazole 0.75%
Na2MoO4 1.62%Na 2 MoO 4 1.62%
ZnSO4 2.50% ZnSO4 2.50%
水 70.62%。Water 70.62%.
实施例9Example 9
配制过程:配制环保型复合预膜剂A剂、B剂各100.00gPreparation process: prepare 100.00g each of environment-friendly composite pre-film agent A and B
A剂的配制:将50.00g固含量为50%的2-膦酸基-1,2,4-三羧酸丁烷(PBTCA)、2.00g固含量为30%的丙烯酸/2-甲基-2′-丙稀酰胺基丙烷磺酸/丙烯酸羟丙酯三元共聚物(AA/AMPS/HPA)、39.10g的水混合搅拌均匀,再加入8.90g七水硫酸锌搅拌溶解,即得到所需配制的100.00g A剂。Preparation of Agent A: 50.00g of 2-phosphonic acid-1,2,4-tricarboxylic butane (PBTCA) with a solid content of 50%, 2.00g of acrylic acid/2-methyl-butane with a solid content of 30% 2'-acrylamidopropanesulfonic acid/hydroxypropyl acrylate terpolymer (AA/AMPS/HPA), 39.10g of water were mixed and stirred evenly, then 8.90g of zinc sulfate heptahydrate was added and stirred to dissolve, and the desired The prepared 100.00g agent A.
B剂的配制:将62.50g固含量为40%的聚环氧琥珀酸钠与34.50g水混合并搅拌均匀,再加入1.60g的苯并三氮唑及1.40g的二水钼酸钠(Na2MoO3·2H2O)搅拌溶解,即得到所需配制的100.00gB剂。The preparation of agent B: 62.50g solid content is 40% sodium polyepoxysuccinate and 34.50g water are mixed and stirred evenly, then add 1.60g of benzotriazole and 1.40g of sodium molybdate dihydrate (Na 2 MoO 3 .2H 2 O) was stirred and dissolved to obtain 100.00 g of B agent to be prepared.
将上述配好的药剂溶液A剂和B剂,按重量比A∶B=1∶1的比例直接加入实验用水进行旋转挂片实验,A剂投加200mg·L-1,B剂投加200mg·L-1,实验温度45℃,实验时间48h,实验用水水质为:Ca2+(以CaCO3计)255mg·L-1、总碱度(以CaCO3计)240mg·L-1、Cl- 110mg·L-1、SO4 2-102mg·L-1、pH8.2。预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。Add agent A and agent B of the above-mentioned prepared agent solution directly to the test water in the ratio of weight ratio A:B=1:1 to carry out the rotating test, add 200mg·L -1 to agent A, and add 200mg to agent B ·L -1 , the experimental temperature is 45°C, the experimental time is 48h, the water quality of the experimental water is: Ca 2+ (calculated as CaCO 3 ) 255mg·L -1 , total alkalinity (calculated as CaCO 3 ) 240mg·L -1 , Cl - 110 mg·L -1 , SO 4 2- 102 mg·L -1 , pH 8.2. After the pre-film was finished, it was tested with copper sulfate standard drop solution. The experimental results are shown in Table 1.
以一种预膜剂的投加量400mg·L-1(A剂200mg·L-1,B剂200mg·L-1)为基础计算,其重量百分比如下:Based on the dosage of a pre-film agent of 400mg·L -1 (a dose of 200mg·L -1 , B dose of 200mg·L -1 ), the weight percentage is as follows:
PBTCA 12.50%PBTCA 12.50%
PESA 12.50%PESA 12.50%
AA/AMPS/HPA 0.30%AA/AMPS/HPA 0.30%
苯并三氮唑 0.80%Benzotriazole 0.80%
Na2MoO4 0.60%Na 2 MoO 4 0.60%
ZnSO4 2.50% ZnSO4 2.50%
水 70.80%。Water 70.80%.
对比例comparative example
按六偏磷酸钠170mg·L-1、硫酸锌80mg·L-1、AA/AMPS/HPA共聚物30mg·L-1的药剂浓度加入实验用水进行旋转挂片预膜实验,实验用水水质为:Ca2+(以CaCO3计)125mg·L-1、总碱度(以CaCO3计)150mg·L-1、Cl- 78mg·L-1、SO4 2-98mg·L-1、pH8.0。实验时用氨基磺酸控制实验水质的pH为5.5~6.5,实验温度45℃,实验时间48h,预膜结束后用硫酸铜标准点滴液检验,实验结果见表1。According to the concentration of sodium hexametaphosphate 170mg·L -1 , zinc sulfate 80mg·L -1 , and AA/AMPS/HPA copolymer 30mg·L -1 , the test water was added to carry out the pre-film test of the rotary hanging film. The quality of the test water is: Ca2 + (calculated as CaCO 3 ) 125mg·L -1 , total alkalinity (calculated as CaCO 3 ) 150mg·L -1 , Cl - 78mg·L -1 , SO 4 2- 98mg·L -1 , pH8.0 . During the experiment, sulfamic acid was used to control the pH of the experimental water to 5.5-6.5, the experimental temperature was 45°C, and the experimental time was 48 hours.
表1实验结果Table 1 Experimental results
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Cited By (20)
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CN101928077A (en) * | 2010-08-30 | 2010-12-29 | 天津精华石化有限公司 | Low-phosphorus corrosion and scale inhibitor |
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Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US5256332A (en) * | 1992-11-19 | 1993-10-26 | Betz Laboratories, Inc. | Method of inhibiting corrosion in aqueous systems |
CN100434376C (en) * | 2006-10-12 | 2008-11-19 | 同济大学 | A low-phosphorus environment-friendly composite corrosion and scale inhibitor for treating circulating cooling water and its application method |
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