CN1243833A - Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process - Google Patents

Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process Download PDF

Info

Publication number
CN1243833A
CN1243833A CN 99114320 CN99114320A CN1243833A CN 1243833 A CN1243833 A CN 1243833A CN 99114320 CN99114320 CN 99114320 CN 99114320 A CN99114320 A CN 99114320A CN 1243833 A CN1243833 A CN 1243833A
Authority
CN
China
Prior art keywords
sulfonic
nach
polyamine
phosphonic
polyamine compounds
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
Application number
CN 99114320
Other languages
Chinese (zh)
Other versions
CN1074419C (en
Inventor
王锦堂
朱红军
俞斌
杨文忠
刘景宁
张锡琦
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NANJING CHEMICAL UNIV
Original Assignee
NANJING CHEMICAL UNIV
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by NANJING CHEMICAL UNIV filed Critical NANJING CHEMICAL UNIV
Priority to CN99114320A priority Critical patent/CN1074419C/en
Publication of CN1243833A publication Critical patent/CN1243833A/en
Application granted granted Critical
Publication of CN1074419C publication Critical patent/CN1074419C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

A process for preparing polyamine compound containing phosphonic, sulfonic and carboxylic radicals includes such steps as reaction of polyvinyl polyamine on chloroacetic acid to obtain carboxy methyl polyvinylpolyamin hydrochloride as intermediate, reaction of said intermediate on sodium carboxysulfonate to obtain carboxymethyl polyvinylpolyaminosulfonic acid as another intermediate, and reaction of said another intermediate on polyformaldehyde and PCl3 to obtain the product [A(NACH2CH2)nNA2, where n=1-6; A=mCH2PO3H2; m'CH2SO3H; m"CH2CO2H; m, m' or m"=1-n and m+m'+m"=m+[3]]. Said product can be used as anticorrosion scaling-resistant disperser for treating industrial circulated water.

Description

Contain polyamine compounds of phosphonic, sulfonic and carboxylic radicals and preparation method thereof
The present invention relates to a kind of polyfunctional group water conditioner (corrosion inhibiting and descaling agent), particularly a kind of invention that contains phosphonate group-sulfonic group-carboxylic acid group's polyamine compounds.
Because the shortage day by day of Freshwater resources, and metallic corrosion etc. has brought enormous economic loss [Shi Shengtai etc. for the industrial and agricultural production of countries in the world, corrosion and protection, 1990,11 (4): 1], industrial cycle water treatment medicament more and more is subject to people's attention [Jiang Liren, corrosion and protection, 1984, (1)].The organic multicomponent phosphonic acids is a present widely used class water conditioner [GWofford, C Slezak, M Bukay.Industrial Water Treatment, 1991], and they have solved the problem of system's generation calcium carbonate scale, anti-higher temperatures.Its defective is that organic phospho acid can not suppress phosphorus system effectively and phosphorus zinc is calcium phosphate scale, zinc dirt and the ferric oxide deposition problems that produces in the water treatment prescription.The eighties, the co-polymer of sulfonate that contains of domestic and international Application and Development had good restraining ability to calcium phosphate scale, and dispersing iron oxide effectively, stablize zine ion, thereby developing [A Pryor rapidly, M Bukay.Industry Water Treatment, 1991], the polyethylene polyamine polymethylene sulfonate that meanwhile contains single sulfonic acid group obtains research [Yao Cheng etc.Treatment of Industrial Water, 1998, (5): 18], and the introducing sulfonic acid group also obtains research [Han Yinglin etc. in the organic phospho acid molecule.Nanjing University of Chemical Technology's journal, 1997, (3): 7].As everyone knows, contain phosphonate group and carboxylic acid group in the molecule of phosphine carboxylic acid compound, be that a class has the scale inhibition inhibiter in New Year concurrently, many distinctive features are arranged in water quality stabilizer, developed PBTCA (2-phosphonic acid butane-1,2 both at home and abroad at present, the 4-tricarboxylic acid) and HPA (2-hydroxyl phosphine acetate) [Ji Yongliang, Treatment of Industrial Water, 1995, (6): 1].These water conditioners only contain one or both functional groups, all also having some shortcomings aspect the corrosion-mitigation scale-inhibition dispersion, if any scale inhibition effect can, but corrosion mitigating effect is relatively poor, over-all properties is difficult to satisfy the demand, when reality is used, usually want composite use, need to adjust prescription every now and then, make the user very inconvenient in use by the professional.Therefore developing novel polyfunctional group water conditioner easy to use just becomes domestic and international problem demanding prompt solution.
The object of the invention is to develop the polyamine compounds water conditioner that contains phosphonate group-sulfonic group-carboxylic acid group, makes it multiple functional, and is easy to use, and inhibition, scale inhibition, dispersing property are good.
Novel polyfunctional group water conditioner of the present invention is to introduce sulfonic group (SO simultaneously in a molecule 3H), phosphonate group (PO 3H 2) and carboxylic acid group (CO 2H), its concrete structure is as follows:
Figure A9911432000051
(n=1~6; A=m CH 2PO 3H 2M ' CH 2SO 3H; M " CH 2CO 2H; M, m ', m "=1~n; M+m '+m "=n+3) make product have inhibition preferably, scale inhibition, dispersing property simultaneously, and can produce based on inhibition or with scale inhibition according to the water quality needs and be separated into main product, to remedy the deficiency of currently available products performance.
Preparation method's the first step is: drip the chloroacetic aqueous solution of 1~7mol in the aqueous solution of 1mol polyethylene polyamine, dropwise the back and reacted 4~12 hours down at 20~90 ℃, get intermediate carboxymethyl polyethylene polyamine hydrochloride [A (NACH 2CH 2) nNA 2(HCl) M "(II), n=1~6; A=m " (CH 2CO 2H), (n+3-m ") H].
Second step was: to intermediate (II) in, add a certain amount of NaOH and regulate pH to 3~9, add 1~7mol sodium hydroxymethane sulfonate again, 20~100 ℃ of reactions 4~12 hours down, intermediate carboxymethyl polyethylene polyamine base is pitched sulfonic acid [A (NACH 2CH 2) nNA 2(III), n=1~6; A=m " (CH 2CO 2H), m ' (CH 2SO 3H), (n+3-m '-m ") H].
The 3rd step was: add 1~9mol Paraformaldehyde 96 in intermediate (III), and drip 1~8mol phosphorus trichloride, reacted 4~18 hours down at 20~120 ℃ then, get product carboxymethyl methylenephosphonic acid polyethylene polyamine base methylsulfonic acid [A (NACH 2CH 2) nNA 2(I), n=1~6; A=mCH 2PO 3H 2M ' CH 2SO 3H; M " CH 2CO 2H; M, m ', m "=1~n; M+m '+m "=n+3].
Its synthetic route is as follows:
Figure A9911432000061
(n=1~6; A=m CH 2PO 3H 2M ' CH 2SO 3H; M " CH 2CO 2H; M, m ', m "=1~n; M+m '+m "=n+3)
Above synthetic route is simple, and raw material is easy to get, and cost is low." synergistic effect " between institute's synthetic product utilization phosphonate group, sulfonic group and the carboxylic acid group, make its inhibition, scale inhibition, dispersing property better, and the different products of forming have different characteristics at aspects such as inhibition, scale inhibition, dispersions, thereby can adapt to various requirements in water quality, extensively in handling, uses industrial circulating cooling water.Therefore exploitation, the promotion and application of polyfunctional group water conditioner of the present invention have bigger social benefit and economic benefit.
Embodiment: embodiment 1, preparation N, N '-two methene phosphonic acids-N '-methene sulfonic acid-N-acetoxyl quadrol (CSDPE):
1.1 frozen water cooling down to quadrol (30g 0.5mol) and drip the chloroacetic aqueous solution (the 47.3g Mono Chloro Acetic Acid is dissolved in the 40ml water) in the mixture of 40ml water, dropwises the back 65~90 ℃ of reactions 6 hours down, intermediate carboxymethyl ethylenediamine-hydrochloride [H 2NCH 2CH 2NH 2(CH 2CO 2H) Cl (CE)] aqueous solution.
1.2 adding HCl adjusting pH in the aqueous solution of the said products is 5.8, adds 67g hydroxymethyl sodium sulfonate again, reacts down at 80~90 ℃ promptly to get intermediate carboxymethyl quadrol base methene sulfonic acid [HO in 7 hours 3SCH 2NHCH 2CH 2NHCH 2CO 2H (CSE)] aqueous solution.
1.3 in above-mentioned solution, add the 40g Paraformaldehyde 96, the frozen water cooling drips phosphorus trichloride 87.6ml (1.0mol) down, after dropwising, be warming up to 80~90 ℃ gradually, and after 12 hours, be cooled to filtering precipitation after the room temperature in reaction under this temperature, N, the aqueous solution 200g of N '-two methene phosphonic acids-N '-methene sulfonic acid-N-acetoxyl quadrol (CSDPE) concentrates and separates out CSDPE 168g (total recovery is 84%) under the effect of methyl alcohol.Product is through methanol-water recrystallization, results of elemental analyses: C:21.23, H:4.64, N:6.88 (theoretical value is C:21.01, H:4.53, N:7.00).This product is through static-state scale inhibition test, and the result shows under 2ppm concentration, can reach 85.4% to the scale inhibition performance of calcium carbonate scale; Corrosion inhibition test shows that the concentration of this product in tap water is that 5ppm is 99.4% to the carbon steel corrosion inhibition rate.Embodiment 2, preparation N-methylenephosphonic acid-N '-methene sulfonic acid-N, N '-diacetoxyl quadrol (DCSPE):
2.1 the frozen water cooling is down to quadrol (30g, 0.5mol) and the mixture of 40ml water in drip the chloroacetic aqueous solution (the 94.6g Mono Chloro Acetic Acid is dissolved in the 80ml water), dropwise the back and reacted 9 hours down, get intermediate dicarboxyl methyl ethylenediamine hydrochloride [HO at 70~90 ℃ 2CCH 2NHCH 2CH 2NH 2(CH 2CO 2H) Cl (DCE)] aqueous solution.
2.2 adding NaOH adjusting pH in the aqueous solution of the said products is 7.6, adds 67g hydroxymethyl sodium sulfonate again, reacts down at 70~100 ℃ promptly to get intermediate carboxymethyl quadrol base methene sulfonic acid [HO in 7 hours 3SCH 2(HO 2CCH 2) NCH 2CH 2NHCH 2CO 2H (DCSE)] aqueous solution.
2.3 in above-mentioned solution, add the 20g Paraformaldehyde 96, the frozen water cooling drips phosphorus trichloride 43.8ml (0.55mol) down, after dropwising, be warming up to 70~100 ℃ gradually, and after 7 hours, be cooled to filtering precipitation after the room temperature in reaction under this temperature, N-two methene phosphonic acids-N '-methene sulfonic acid-N, the aqueous solution 181g of N '-diacetoxyl quadrol (DCSPE) (contain DCSPE 150g, total recovery is 83%).This product is through static-state scale inhibition test, and the result shows under 2ppm concentration, can reach 87.3% to the scale inhibition performance of calcium carbonate scale; Corrosion inhibition test shows that the concentration of this product in tap water is that 5ppm is 99.0% to the carbon steel corrosion inhibition rate.Embodiment 3, preparation N-methylenephosphonic acid-N, N '-two methene sulfonic acid-N-acetoxyl quadrol (CDSPE):
3.1 adding HCl adjusting pH in the aqueous solution of 1.1 products is 6.7, adds 134g hydroxymethyl sodium sulfonate again, reacts down at 60~90 ℃ promptly to get intermediate carboxymethyl quadrol base methene sulfonic acid [HO in 9 hours 3SCH 2NHCH 2CH 2N (CH 2SO 3H) CH 2CO 2H (CDSE)] aqueous solution.
3.2 in above-mentioned solution, add the 20g Paraformaldehyde 96, the frozen water cooling drips phosphorus trichloride 43.8ml (0.5mol) down, after dropwising, be warming up to 60~90 ℃ gradually, and after 9 hours, be cooled to filtering precipitation after the room temperature in reaction under this temperature, N, the aqueous solution 200g of N '-two methene phosphonic acids-N '-methene sulfonic acid-N-acetoxyl quadrol (CDSPE) (contain CDSPE 162g, total recovery is 81%).This product is through static-state scale inhibition test, and the result shows under 2ppm concentration, can reach 90.1% to the scale inhibition performance of calcium carbonate scale; Corrosion inhibition test shows that the concentration of this product in tap water is that 5ppm is 99.1% to the carbon steel corrosion inhibition rate.Embodiment 4, preparation N, N ', N "-three methene phosphonic acids-N "-methene sulfonic acid-N-acetoxyl diethylenetriamine (CSDPE):
4.1 the frozen water cooling is down to diethylenetriamine (51.5g, 0.5mol) and the mixture of 50ml water in drip the chloroacetic aqueous solution (the 47.3g Mono Chloro Acetic Acid is dissolved in the 50ml water), dropwise the back and reacted 6 hours down, get intermediate carboxymethyl diethylenetriamine hydrochloride [H at 40~85 ℃ 2NCH 2CH 2NHCH 2CH 2NH 2(CH 2CO 2H) Cl (CE)] aqueous solution.
4.2 adding HCl adjusting pH in the aqueous solution of the said products is 7, adds 67g hydroxymethyl sodium sulfonate again, reacts down at 40~85 ℃ promptly to get intermediate carboxymethyl quadrol base methene sulfonic acid [HO in 6 hours 3SCH 2NHCH 2CH 2NHCH 2CO 2H (CSE)] aqueous solution.
4.3 in above-mentioned solution, add the 60g Paraformaldehyde 96, the frozen water cooling drips phosphorus trichloride 131.4ml (1.2mol) down, after dropwising, be warming up to 60~90 ℃ gradually, and after 16 hours, be cooled to filtering precipitation after the room temperature in reaction under this temperature, get N, N ', N " aqueous solution 270g (contain CSDPE 205g, total recovery is 81%) of-three methene phosphonic acids-N '-methene sulfonic acid-N-acetoxyl diethylenetriamine (CSDPE).This product is through static-state scale inhibition test, and the result shows under 2ppm concentration, can reach 86.0% to the scale inhibition performance of calcium carbonate scale; Corrosion inhibition test shows that the concentration of this product in tap water is that 5ppm is 99.6% to the carbon steel corrosion inhibition rate.
Synthesis condition, result and the performance of other intermediate (II), intermediate (III) and the finished product sees Table 1 respectively, table 2, table 3 and table 4.
Synthesis condition, the result of table 1 intermediate (II)
Sequence number ????A(NACH 2CH 2) nNA 2(HCl) m”(I) ????A=m”(CH2CO2H),(n+3-m”)H ????n/m” Mol ratio polyethylene polyamine/Mono Chloro Acetic Acid Temperature ℃ Reaction times Productive rate %
??1 ????1/1 ????1∶1 ??65-90 ????6h ????92
??2 ????1/2 ????1∶2.1 ??70-90 ????10h ????89
??3 ????2/1 ????1∶1 ??40-85 ????6h ????93
??4 ????2/2 ????1∶2 ??20-85 ????6h ????90
??5 ????3/1 ????1∶1 ??30-70 ????6h ????91
??6 ????4/1 ????1∶1 ??20-60 ????4h ????93
??7 ????5/2 ????1∶2.2 ??20-70 ????6h ????94
??8 ????6/3 ????1∶3.2 ??70-90 ????12h ????89
Synthesis condition, the result of table 2 intermediate (III)
Sequence number ????A(NACH 2CH 2) nNA 2(III) ??A=m”(CH2CO2H),m’CH 2SO 3H, ????(n+3-m’-m”)H ????n/m’/m” Mol ratio I/HO 3SCH 2OH Temperature ℃ Reaction times Productive rate %
???1 ????1/1/1 ????1∶1 ??80-90 ??7h ????92
???2 ????1/1/2 ????1∶1 ??70-100 ??7h ????89
???3 ????1/2/1 ????1∶2.1 ??60-90 ??9h ????87
???4 ????2/1/1 ????1∶1 ??40-85 ??6h ????93
???5 ????2/2/1 ????1∶2.1 ??65-100 ??10h ????86
???6 ????2/1/2 ????1∶2 ??20-85 ??6h ????90
???7 ????3/1/1 ????1∶1 ??30-70 ??6h ????91
???8 ????3/2/1 ????1∶2.1 ??70-90 ??9h ????88
???9 ????3/1/2 ????1∶1 ??40-100 ??9h ????89
??10 ????4/1/1 ????1∶1 ??40-90 ??9h ????91
??11 ????4/3/1 ????1∶3.4 ??50-100 ??12h ????86
??12 ????5/1/2 ????1∶1 ??40-90 ??8h ????92
??13 ????5/3/2 ????1∶3.4 ??60-90 ??12h ????86
??14 ????6/3/3 ????1∶3.4 ??60-90 ??12h ????86
Synthesis condition, the result of table 3 the finished product (I)
Sequence number ????A(NACH 2CH 2) nNA 2??(I) ?A=m”(CH 2CO 2H),m’(CH 2SO 3H), ????m(CH 2PO 3H 2) ????n/m/m’/m” Mol ratio II/ (CH 2O) n/PCl 3 Temperature ℃ Reaction times Productive rate %
??1 ????1/2/1/1 ????1∶3∶2.1 ??80-90 ??12h ????92
??2 ????1/1/1/2 ????1∶1.5∶1.1 ??70-100 ??7h ????89
??3 ????1/1/2/1 ????1∶1.5∶1.1 ??60-90 ??9h ????87
??4 ????2/3/1/1 ????1∶4.1∶3.2 ??40-85 ??16h ????93
??5 ????2/2/2/1 ????1∶3∶2.1 ??65-100 ??10h ????86
??6 ????2/2/1/2 ????1∶3∶2.1 ??20-85 ??8h ????90
??7 ????3/4/1/1 ????1∶5.2∶4.3 ??30-70 ??18h ????91
??8 ????3/3/2/1 ????1∶4.1∶3.2 ??50-110 ??16h ????86
??9 ????3/3/1/2 ????1∶4.1∶3.2 ??40-110 ??12h ????90
?10 ????4/5/1/1 ????1∶7∶5.6 ??40-80 ??14h ????91
?11 ????4/3/3/1 ????1∶4.1∶3.2 ??50-100 ??12h ????86
?12 ????5/5/1/2 ????1∶7∶5.6 ??40-90 ??14h ????92
?13 ????5/3/3/2 ????1∶4.1∶3.2 ??60-110 ??16h ????86
?14 ????6/3/3/3 ????1∶4.1∶3.2 ??40-120 ??18h ????86
The performance of table 4 sintetics (I)
Sequence number ????A(NACH 2CH 2) nNA 2(I) ?A=m”(CH 2CO 2H),m’(CH 2SO 3H),m(CH 2PO 3H 2) ????n/m/m’/m” Corrosion inhibition rate a????% Scale inhibition performance b??(CaCO 3) ????% Stablize zinc c????%
??1 ????1/2/1/1 ????99.4 ????85.4 ????82.4
??2 ????1/1/1/2 ????99.0 ????87.3 ????88.8
??3 ????1/1/2/1 ????99.1 ????90.1 ????89.1
??4 ????2/3/1/1 ????99.6 ????86.0 ????89.4
??5 ????2/2/2/1 ????99.4 ????92.0 ????90.1
??6 ????2/2/1/2 ????99.4 ????91.8 ????93.5
??7 ????3/4/1/1 ????99.7 ????90.5 ????89.2
??8 ????3/3/2/1 ????99.6 ????95.4 ????93.3
??9 ????3/3/1/2 ????99?6 ????93.7 ????94.7
??10 ????4/5/1/1 ????99.9 ????91.9 ????90.6
??11 ????4/3/3/1 ????99.8 ????95.3 ????94.2
??12 ????5/5/1/2 ????99.9 ????94.9 ????96.2
??13 ????5/3/3/2 ????99.8 ????99.1 ????99.5
??14 ????6/3/3/3 ????99.8 ????99.6 ????99.8
A: drug concentration is 5mg/L; B: drug concentration is 2mg/L; C: drug concentration is 10mg/L.

Claims (4)

1 one kinds of polyamine compounds that contain phosphonic, sulfonic and carboxylic radicals is characterized in that containing simultaneously in the molecule phosphonate group, sulfonic group and carboxylic acid group's polyamine compounds, and it has following general formula: A (NACH 2CH 2) NA 2(I), n=1~6 wherein; A=m CH 2PO 3H 2M ' CH 2SO 3H; M " CH 2CO 2H; M, m ', m "=1~n; M+m '+m "=n+3.
2 contain the preparation method of the polyamine compounds of phosphonic, sulfonic and carboxylic radicals, it is characterized in that the first step, in the aqueous solution of every 1mol polyethylene polyamine, drip the chloroacetic aqueous solution of 1~7mol, dropwise the back and reacted 4~12 hours down, get intermediate carboxymethyl polyethylene polyamine hydrochloride [A (NACH at 20~90 ℃ 2CH 2) nNA 2(HCl) M "(II), n=1~6; A=m " (CH 2CO 2H), (n+3-m ") H].Second step was: adding NaOH or HCl regulate pH in intermediate (II), and pH is 3~9 in control, adds 1~7mol sodium hydroxymethane sulfonate again, and reaction is 4~12 hours under 20~100 ℃, get intermediate carboxymethyl polyethylene polyamine base fork sulfonic acid [A (NACH 2CH 2) nNA 2(III), n=1~6; A=m " (CH 2CO 2H), m ' (CH 2SO 3H), (n+3-m '-m ") H].The 3rd step was: add 1~9mol Paraformaldehyde 96 in intermediate (III), and drip 1~8mol phosphorus trichloride, reacted 4~18 hours down at 20~120 ℃ then, get product carboxymethyl methylenephosphonic acid polyethylene polyamine base methylsulfonic acid [A (NACH 2CH 2) nNA 2(I), n=1~6; A=m CH 2PO 3H 2M ' CH 2SO 3H; M " CH 2CO 2H; M, m ', m "=1~n; M+m '+m "=n+3].
3 preparation methods that contain the polyamine compounds of phosphonic, sulfonic and carboxylic radicals according to claim 2 is characterized in that the optimal ph in second step is 3~9.
4 contain the polyamine compounds A (NACH of phosphonic, sulfonic and carboxylic radicals 2CH 2) NA 2(n=1~6 wherein; A=m CH 2PO 3H 2M ' CH 2SO 3H; M " CH 2CO 2H; M, m ', m "=1~n; M+m '+m "=n+3) make inhibiter, Scale inhibitors, dispersive purposes at industrial circulating cooling water as water conditioner.
CN99114320A 1999-07-12 1999-07-12 Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process Expired - Fee Related CN1074419C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN99114320A CN1074419C (en) 1999-07-12 1999-07-12 Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN99114320A CN1074419C (en) 1999-07-12 1999-07-12 Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process

Publications (2)

Publication Number Publication Date
CN1243833A true CN1243833A (en) 2000-02-09
CN1074419C CN1074419C (en) 2001-11-07

Family

ID=5277420

Family Applications (1)

Application Number Title Priority Date Filing Date
CN99114320A Expired - Fee Related CN1074419C (en) 1999-07-12 1999-07-12 Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process

Country Status (1)

Country Link
CN (1) CN1074419C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1100059C (en) * 2000-05-19 2003-01-29 中国石油化工集团公司 Sulfonic acid-containing organic phosphine carboxylic acid compound and its prepn. and application
CN100360546C (en) * 2004-10-20 2008-01-09 西南师范大学 Process for one-pot preparation of chloromethyl monosodium phosphonate
CN102321462A (en) * 2011-06-14 2012-01-18 北京科技大学 Method for preparing pH regulating stabilizer of oil gas field

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5534611A (en) * 1993-10-29 1996-07-09 Nalco Chemical Company Sulfonated and carboxylated aminoethylenephosphonic acid and aminobis (methylene) phosphinic acid

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1100059C (en) * 2000-05-19 2003-01-29 中国石油化工集团公司 Sulfonic acid-containing organic phosphine carboxylic acid compound and its prepn. and application
CN100360546C (en) * 2004-10-20 2008-01-09 西南师范大学 Process for one-pot preparation of chloromethyl monosodium phosphonate
CN102321462A (en) * 2011-06-14 2012-01-18 北京科技大学 Method for preparing pH regulating stabilizer of oil gas field
CN102321462B (en) * 2011-06-14 2013-07-03 北京科技大学 Method for preparing pH regulating stabilizer of oil gas field

Also Published As

Publication number Publication date
CN1074419C (en) 2001-11-07

Similar Documents

Publication Publication Date Title
CN101607766B (en) Preparation of corrosion and scale inhibitor used for high alkaline high chlorine circulating cooling water
CN101757761B (en) Method for treating glyphosate mother liquor by oxidation method
CN101830580A (en) Method for treating glyphosate mother solution by using oxidization method
CN101700937A (en) Composite scale inhibitor
CN103242365B (en) A kind of preparation of branch-shape polymer polyamide-amide eight methylene phosphonic acid and application thereof
CN103254228A (en) Preparation method and application of dendritic polymer ethanediamine nuclear polyamide octo-methanephosphonic acid
CN101503426B (en) Novel technique for coproduction of 2-phosphonobutane-1,2,4-tricabroxylic acid and methyl chloride
CN1850740A (en) Method for producing nitrgen-phosphor-magnesium long-service slow-release composite fertilizer containing rare-eanth
CN1074419C (en) Polyamine compounds containing phosphonic, sulfonic and carboxylic radicals and their preparing process
CN105036365A (en) Draught fan dedusting stripping scale inhibitor and preparation method thereof
CN105060515A (en) Scale inhibitor for preventing deposition of barium and strontium scales, and preparation method thereof
CN105439299A (en) Method for preparing hyperbranched polyethyleneimine copolymer water treatment agent and application of hyperbranched polyethyleneimine copolymer water treatment agent
CN101792463B (en) Nitrogen-containing aryl hypophosphorous acid metal salt and preparation method thereof
CN1307113C (en) Environmental-protection high-efficiency low-phosphonic scale inhibitor composition and its preparation method and use
CN103232118A (en) Sodium lignin sulfonate compound corrosion and scale inhibitor and preparation method thereof
CN103708637A (en) Amino trimethylene phosphonic acid-N-oxide and preparation method thereof
CN101497480B (en) Novel industrial water treatment agent and preparation thereof
CN100469714C (en) Composite water treating agent for central air conditioner freezing water
CN105585143A (en) Scale inhibitor for industrial water treatment and preparation method and application method thereof
CN108641046B (en) Preparation of environment-friendly efficient water quality stabilizer RG-15
CN104692546B (en) A kind of demineralized water water treatment agent and its preparation method and application
CN111807527A (en) Strontium-barium scale inhibitor for oil field water treatment and preparation method thereof
CN109607833A (en) A kind of formula and its application method of corrosion inhibiting and descaling agent
CN104628156A (en) Phosphorus-free descaling corrosion inhibitor
CN102070664A (en) Arsenic removal process for amino trimethylene phosphonic acid

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee