DK169709B1 - Corrosion Inhibition Method - Google Patents
Corrosion Inhibition Method Download PDFInfo
- Publication number
- DK169709B1 DK169709B1 DK150787A DK150787A DK169709B1 DK 169709 B1 DK169709 B1 DK 169709B1 DK 150787 A DK150787 A DK 150787A DK 150787 A DK150787 A DK 150787A DK 169709 B1 DK169709 B1 DK 169709B1
- Authority
- DK
- Denmark
- Prior art keywords
- acid
- weight
- polymer
- corrosion
- process according
- Prior art date
Links
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
- C23F11/10—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 using organic inhibitors
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Magnetic Heads (AREA)
- Internal Circuitry In Semiconductor Integrated Circuit Devices (AREA)
- Prevention Of Electric Corrosion (AREA)
- Iron Core Of Rotating Electric Machines (AREA)
Abstract
Description
XX
DK 169709 B1DK 169709 B1
Opfindelsen angår en fremgangsmåde til inhibering af korrosion i industrielt kølevand, der har en relativt høj hårdhed og et pH på mindst 8.The invention relates to a method for inhibiting corrosion in industrial cooling water having a relatively high hardness and a pH of at least 8.
5 Betegnelsen "phosphonat" refererer til organiske materiale, der indholder 1 eller flere -PO^^ grupper, og salte deraf.The term "phosphonate" refers to organic matter containing 1 or more -PO 2 groups and salts thereof.
Phosphonater, der er særligt anvendelige ved opfindelsen, 10 omfatter 1-hydroxy-1,1-ethan-diphosphonsyre (HEDP), 2- phosphonobutan-1,2,4-tricarboxylsyre (PBTC), amino-tris-methylenphosphonsyre (AMP) og deres salte. Koncentrationerne og doseringsniveauerne og/eller intervallerne for polymere, phophonater og midler er anført i deres aktive 15 tilstande.Phosphonates particularly useful in the invention include 1-hydroxy-1,1-ethane diphosphonic acid (HEDP), 2-phosphonobutane-1,2,4-tricarboxylic acid (PBTC), amino-tris-methylene phosphonic acid (AMP) and their salts. The concentrations and dosage levels and / or ranges of polymers, phophonates and agents are listed in their active states.
Der forekommer korrosion, når metaller oxideres til deres tilsvarende ioner og/eller uopløselige salte. F. eks.Corrosion occurs when metals are oxidized to their corresponding ions and / or insoluble salts. For example.
kan korrosion af metallisk jern involvere konvertering 20 til opløseligt jern i et iltningstrin af +2 eller +3 eller til uopløselige jernoxider og -hydroxider. Korrosionen har også en tosidig natur i den forstand, at en del af metaloverfladen er fjernet, mens dannelsen af uopløselige salte bidrager til opbygningen af udfældninger. Me-25 taltab frembringer nedbrydning af den strukturelle inte gritet i systemet. Der kan slutteligt forekomme lækage mellem vandsystemet og processtrømmene.For example, corrosion of metallic iron may involve conversion 20 to soluble iron in an oxygenation step of +2 or +3 or to insoluble iron oxides and hydroxides. Corrosion also has a two-sided nature in the sense that part of the metal surface is removed, while the formation of insoluble salts contributes to the formation of precipitates. Metal loss produces degradation of the structural integrity of the system. Finally, leakage may occur between the water system and the process streams.
Det er kendt, at korrosion af jern i oxiderende vandmas-30 ser forekommer i henhold til følgende sammenkoblede elektrokemiske processer: 35 DK 169709 B1 2 o 2+ - (1) Fe° ---> Fe + 2e~ (anodisk reaktion) (2) °2 + ^e~ —> 20H_ (katodisk reaktion)It is known that corrosion of iron in oxidizing water masses occurs according to the following interconnected electrochemical processes: (1) Fe ° ---> Fe + 2e ~ (anodic reaction) ( 2) ° 2 + + e ~ -> 20H_ (cathodic reaction)
Inhibering af metalkorrosion af oxiderende vandmasser in-5 volverer typisk dannelsen af beskyttende barrierer på me-taloverfladen. Disse barrierer forhindrer, at oxygen når metaloverfladen og frembringer metaloxidation. For at fungere som korrosionsinhibitor må et kemisk additiv fremme denne proces på en sådan måde, at der dannes og 10 bibeholdes en oxygen-impermeabel barriere. Dette kan gøres ved interaktion med enten den katodiske eller anodis-ke halvcellereaktion.Inhibition of metal corrosion by oxidizing water masses typically involves the formation of protective barriers on the metal surface. These barriers prevent oxygen from reaching the metal surface and produce metal oxidation. In order to act as a corrosion inhibitor, a chemical additive must promote this process in such a way as to create and maintain an oxygen-impermeable barrier. This can be done by interacting with either the cathodic or anodic half-cell reaction.
Inhibitorer kan påvirke den anodiske reaktion 1 ved at få 2+ 15 det resulterende Fe til at danne en impermeabel barriere, hvorved man forhindrer yderligere korrosion. Dette kan gøres ved at inkorporere bestanddele i inhibitorfor- 2+ bindelsen, som: reagerer direkte med Fe , hvorved det 2+ 3+ bundfælder, letter oxidationen af Fe til Fe , hvis 20 forbindelser typisk er mindre opløselige, eller fremmer 3+ dannelsen af uopløselige forbindelser af Fe .Inhibitors can affect the anodic reaction 1 by causing 2+ 15 of the resulting Fe to form an impermeable barrier, thereby preventing further corrosion. This can be done by incorporating constituents into the inhibitor compound, which: reacts directly with Fe, thereby precipitating 2+ 3+ precipitates, facilitating the oxidation of Fe to Fe, whose 20 compounds are typically less soluble, or promoting 3+ formation of insoluble compounds of Fe.
Reduktionen af oxygen ved korrosionskatoder tilvejebringer et andet middel, ved hvis hjælp inhibitorer kan fun-25 gere. Reaktion 2 repræsenterer den halvcelle, hvori oxygen reduceres under korrosionsprocessen. Produktet af denne reaktion er hydroxylionen (0H~). På grund af hydro-xylproduktionen er pH ved overfladen af metaller, der udsættes for korrosion hidrørende fra oxygen, generelt 30 meget større end for det omgivende mediums vedkommende. Mange forbindelser er mindre opløselige ved højere værdier af pH. Disse forbindelser kan bundfælde ved korrosionskatoder og fungere som effektive inhibitorer for korrosion, hvis deres bundfældede form er impermeabel 35 overfor oxygen og er elektrisk ikke ledende.The reduction of oxygen by corrosion cathodes provides another means by which inhibitors can function. Reaction 2 represents the half-cell in which oxygen is reduced during the corrosion process. The product of this reaction is the hydroxyl ion (OH). Due to hydroxyl production, the pH of the surface of metals subjected to corrosion from oxygen is generally much higher than that of the surrounding medium. Many compounds are less soluble at higher pH values. These compounds can precipitate by corrosion cathodes and act as effective inhibitors of corrosion if their precipitated form is impermeable to oxygen and is electrically nonconductive.
Korrosionsinhibitorer fungerer ved at skabe et miljø, DK 169709 B1 3 hvori korrosionsprocessen inducerer inhiberende reaktioner på metaloverfladen. For at et inhiberende middel skal kunne fungere effektivt må midlets komponenter ikke bundfælde under de betingelser, der hersker størstedelen af 5 mediet. Inhibitorer, der på effektiv måde inhiberer denne bundfældning ved kinetisk inhibering, er blevet udførligt beskrevet i litteraturen. Et eksempel af denne type er US patentskrift nr. 3 880 765, som beskriver anvendelsen af polymere til forhindring af bundfældning af calciumcarbo-10 nat.Corrosion inhibitors function by creating an environment in which the corrosion process induces inhibitory reactions to the metal surface. In order for an inhibitory agent to function effectively, the components of the agent must not settle under the conditions prevailing for most of the medium. Inhibitors that effectively inhibit this precipitation by kinetic inhibition have been extensively described in the literature. An example of this type is U.S. Patent No. 3,880,765, which describes the use of polymers to prevent calcium carbonate precipitation.
Anvendelsen af uorganiske phosphater og phosphonater i forbindelse med en tærskelinhibitor for at kontrollere korrosion hidrørende fra oxiderende vandmasser er beskre-15 vet i US patent skrift nr. 4 303 568. Denne metode er yderligere beskrevet i US patentskrift nr. 4 443 340, der beskriver, at en blanding, der udelukkende omfatter uorganiske phosphater og en polymer inhibitor, har gode egenskaber i tilstedeværelse af opløst jern.The use of inorganic phosphates and phosphonates in conjunction with a threshold inhibitor to control corrosion resulting from oxidizing water masses is described in U.S. Patent No. 4,303,568. This method is further described in U.S. Patent No. 4,443,340, which describes , that a mixture comprising exclusively inorganic phosphates and a polymeric inhibitor has good properties in the presence of dissolved iron.
2020
Man kan opnå korrosionsinhibering ved en kombination af anvendelsen af inhibitorer og modifikation af mediets kemi. US patentskrift nr. 4 547 540 beskriver en metode til korrosionsinhibering, der omfatter drift under betingel-25 ser omfattende højt pH og alkalinitet. Denne metode beror ikke på anvendelsen af uorganiske phosphater, idet den tilvejebringer et produkt, der fra et miljømæssigt synspunkt er mere ønskværdigt.Corrosion inhibition can be achieved by a combination of the use of inhibitors and modification of the chemistry of the medium. U.S. Patent No. 4,547,540 discloses a method of corrosion inhibition comprising operating under conditions comprising high pH and alkalinity. This method does not depend on the use of inorganic phosphates, since it provides a product which is more desirable from an environmental point of view.
30 I FR patentskrift nr. 1 598 419 er beskrevet en fremgangsmåde til forhindring af kedelstensdannelse og korrosion i kølevandssystemer, hvilken fremgangsmåde består i at tilføre sådanne systemer et middel indeholdende en vandopløselig organisk polymer og et organisk phosphon-35 syrederivat. Som eksempel på en vandopløselig polymer nævnes bl. a. acrylamid/acrylsyre-copolymere.30 In FR patent specification No. 1 598 419, a process for preventing scaling and corrosion in cooling water systems is described, which consists in supplying such systems with an agent containing a water-soluble organic polymer and an organic phosphonic acid derivative. An example of a water-soluble polymer is mentioned, among others. a. acrylamide / acrylic acid copolymers.
DK 169709 B1 4 I FR patent skrift nr. 2 235 205 er beskrevet en fremgangsmåde til forhindring af kedelstensdannelse og korrosion i vandtilførselsrør, hvilken fremgangsmåde består i, at der i sådanne rør indføres mindst én phosphoncarboxyl-5 syre og en anden forbindelse, såsom et polyacrylamidde-rivat.DK 169709 B1 4 FR patent specification No. 2,235,205 discloses a method of preventing scaling and corrosion in water supply pipes, which method involves introducing at least one phosphonecarboxylic acid into such pipes and another compound, such as a polyacrylamidde derivative.
I DE patentskrift nr. 3 015 500 er beskrevet en korro-sionsinhiberende sammensætning på basis af en vandopløse-10 lig phosphonsyre, en vandopløselig polymer af acrylsyre, methacrylsyre, maleinsyre eller maleinsyreanhydrid og to-lyltriazol. Som eksempel på en vandopløselig polymer er nævnt copolymere af acrylsyre og acrylamid.DE Patent No. 3,001,500 discloses a corrosion inhibiting composition based on a water-soluble phosphonic acid, a water-soluble polymer of acrylic acid, methacrylic acid, maleic or maleic anhydride, and tolyl triazole. An example of a water-soluble polymer is mentioned copolymers of acrylic acid and acrylamide.
15 Anvendelsen af polymerer med tert.-butylacrylamidgrupper er ikke kendt fra nogen af disse skrifter.The use of polymers with tert-butyl acrylamide groups is not known from any of these publications.
Den foreliggende opfindelse angår en anvendelse af phos-phonatholdige korrosionsinhiberende midler, der indholder 20 en enestående kombination af polymere, phosphonater og den eventuelle anvendelse af aromatiske azoler. Anvendelsen af disse polymere resulterer i signifikant forbedrede egenskaber af korrosionsinhibitorer.The present invention relates to the use of phosphonate-containing corrosion inhibiting agents containing a unique combination of polymers, phosphonates and the optional use of aromatic azoles. The use of these polymers results in significantly improved properties of corrosion inhibitors.
25 Anvendelsen af de copolymere som inhibitorer for kedelsten er diskuteret i US patentskrift nr. 4 566 973. Herfra kendes anvendelse af copolymere, der indeholder tert.-butyl-acrylamid-enheder, men i forbindelse med andre comonomere. Det har nu vist sig, at copolymere in-30 deholdende tert.-butalacrylamidenheder i kombination med calciumphosphonat-inhibitorer er effektive, og at de fungerer effektivt som komponenter i et phosphonatholdigt korrosionsinhiberende middel.The use of the copolymers as inhibitors of scales is discussed in U.S. Patent No. 4,566,973. The use of copolymers containing tert.-butyl-acrylamide units is known, but in connection with other comonomers. It has now been found that copolymers containing tert-butalacrylamide units in combination with calcium phosphonate inhibitors are effective and that they function effectively as components of a phosphonate-containing corrosion inhibitor.
35 Fremgangsmåden ifølge opfindelsen, der er-af den i indledningen til krav 1 angivne art, er ejendommelig ved et i den kendetegnende del af krav 1 angivne.The method according to the invention, which is of the kind set forth in the preamble of claim 1, is characterized by a feature as defined in the characterizing part of claim 1.
DK 169709 B1 5DK 169709 B1 5
Generelt kan man anvende ethvert vandopløseligt phospho-nat, der er i stand til at tilvejebringe korrosionsinhi-bering i alkaliske systemer. I US patentskrift nr.In general, any water-soluble phosphonate capable of providing corrosion inhibition in alkaline systems can be used. In U.S. Pat.
5 4 303 568 findes der en liste af et antal repræsentative phosphonater.5 4 303 568 there is a list of a number of representative phosphonates.
Organophosphonsyreforbindelserne er dem, der har en carbon-til-phosphorbinding, dvs.The organophosphonic acid compounds are those having a carbon-to-phosphorus bond, ie.
10 010 0
IIII
—C—P—OM-C-P-OM
15 OM15 OM
Forbindelser, der ligger inden for omfanget af den før angivne beskrivelse, er generelt omfattet af en af måske tre katagorier, der repræsenteres ved de følgende gene-20 relle formler: 0Compounds which are within the scope of the foregoing description are generally comprised of one of perhaps three categories represented by the following general formulas: 0
IIII
R—p—OMR-P-OM
25 I25 I
OMABOUT
hvori R er lavere alkyl, der har fra 1 - 6 carbonatomer, f. eks. methyl, ethyl, butyl, propyl, isopropyl, pentyl, 30 isopentyl og hexyl; substitueret lavere alkyl med fra 1 -6 carbonatomer, f. eks. hydroxyl- og aminosubstituerede alkyler; et mononucleært aromatisk (aryl-) radikal, f. eks. phenyl, benzen osv., såsom en substitueret mononu-cleær aromatisk forbindelse, f. eks. hydroxyl-, amino-, 35 (lavere alkyl)-substituerede aromater, f,. eks. benzyl-phosphonsyre; og M er en vandopløselig kation, f. eks. natrium, kalium, ammonium, lithium osv. eller hydrogen.wherein R is lower alkyl having from 1 to 6 carbon atoms, for example methyl, ethyl, butyl, propyl, isopropyl, pentyl, isopentyl and hexyl; substituted lower alkyl having from 1 to 6 carbon atoms, for example hydroxyl and amino substituted alkyls; a mononuclear aromatic (aryl) radical, e.g., phenyl, benzene, etc., such as a substituted mononuclear aromatic compound, e.g., hydroxyl, amino, (lower alkyl) -substituted aromatics, e.g. eg benzyl phosphonic acid; and M is a water-soluble cation, e.g., sodium, potassium, ammonium, lithium, etc., or hydrogen.
DK 169709 B1 6DK 169709 B1 6
Specifikke eksempler på forbindelser, der omfattes af denne formel, omfatter: 5 methylphophonsyre CHgPOgl^ ethylphophonsyre CH3CH2P03H2 2 -hydroxyethylphosphonsyre CH2 -CH2 -P03H2Specific examples of compounds encompassed by this formula include: methylphophonic acid CHgPOgl ^ ethylphophonic acid CH3CH2PO3H2 2 -hydroxyethylphosphonic acid CH2 -CH2-PO3H2
10 I10 I
OHOH
2-amino-ethylphosphonsyre CH2-CH2~P03H2 15 NH2 isopropylphosphonsyre CH3 CH3-CH-CH2-P03H2 20 benzen-phosphonsyre CgHg-P03H2 benzylphophonsyre CgHgCH2P03H2 25 0 02-amino-ethylphosphonic acid CH2-CH2 ~ PO3H2 NH2 isopropylphosphonic acid CH3 CH3-CH-CH2-PO3H2 benzene-phosphonic acid CgHg-PO3H2 benzylphophonic acid CgHgCH2PO3H2 25 0 0
II IIII II
M0-P--R1--P-0MM0-P - R 1 - P-0M
I II I
OM OMOM OM
30 hvor er et alkylen med fra 1 til 12 carbonatomer eller et substitueret alkylen med fra 1 til 12 carbonatomer, f. eks. hydroxyl, amino osv. substituerede alkylener, og M er som før defineret.Wherein is an alkylene having from 1 to 12 carbon atoms or a substituted alkylene having from 1 to 12 carbon atoms, e.g. hydroxyl, amino, etc. substituted alkylenes, and M is as previously defined.
Specifikke eksemplificerende forbindelser og deres pågældende formler, der omfattes af den ovenstående formel, er 35 DK 169709 B1 7 som følger: methylen-diphosphonsyre 5 ethyliden-diphosphonsyre H2O3P-CH (CH^) POg^ isopropyliden-diphosphonsyre (CHg)2C(PO^t^)2 1-hydroxy, ethyliden-diphosphonsyre (HEDP) 10Specific exemplifying compounds and their respective formulas encompassed by the above formula are as follows: methylene-diphosphonic acid 5 ethylidene-diphosphonic acid H2O3P-CH (CH2) POg ^ isopropylidene-diphosphonic acid (CHg) 2C (PO t 2) 2 1-hydroxy, ethylidene-diphosphonic acid (HEDP) 10
OHOH
H203P-C(CH3)-P03H2 15 hexamethylen-diphosphonsyre H2°3P-CH2^CH2^4CH2**P03H2 trimethylen-diphosphonsyre H2°3P_(CH2)3"P03H2 decamethylen-diphosphonsyre H2°3P"(CH2)iq~p03H2 20 1-hydroxy, propyliden-diphosphonsyre h2o3pc(oh)ch2(ch3)po3h2 25 1,6-dihydroxy, 1,6-dimethyl, hexamethylen-diphosphonsyre h2o3pc(ch3)(oh)(ch2)4c(ch3)(oh)po3h2 dihydroxy, diethyl-ethylen-diphosphonsyre 30 H203PC (0Η) (C2H5) C (0Η) (C2H5) PO^ 35 DK 169709 B1 8 0 R " R3H203P-C (CH3) -PO3H2 hexamethylene diphosphonic acid H2 ° 3P-CH2 ^ CH2 ^ 4CH2 ** PO3H2 trimethylene diphosphonic acid H2 ° 3P_ (CH2) 3 "PO3H2 decamethylene diphosphonic acid H2 ° 3P" (CH2) iq ~ p0H 1-hydroxy, propylidene diphosphonic acid h2o3pc (oh) ch2 (ch3) po3h2 1,6-dihydroxy, 1,6-dimethyl, hexamethylene diphosphonic acid h2o3pc (ch3) (oh) (ch2) 4c (ch3) (oh) po3h2 dihydroxy, diethyl-ethylene diphosphonic acid 30 H 2 O 3 PC (0Η) (C 2 H 5) C (0Η) (C 2 H 5) PO 2 35 DK 169709 B1 8 0 R "R3
N-R2~P-OMN-R 2 ~ P-ON
5 R4 om hvor R2 er et lavere alkylen med fra 1 til 4 carbonatomer, eller et amin eller hydroxysubstitueret lavere alkylen; R^ er [R2-P0gM2] H, OH, amino, substitueret amino, 10 et alkyl med fra 1-6 carbonatomer, et substitueret al-kyl med fra 1-6 carbonatomer (f. eks. OH, NH2 substitueret) et mononucleært aromatisk radikal og et substitueret mononucleært aromatisk radikal (f. eks. OH, NH2 substitueret); R^ er R^ eller gruppen repræsenteret ved 15 formlen rL) " ° 1 3R 4 is wherein R 2 is a lower alkylene having from 1 to 4 carbon atoms, or an amine or hydroxy substituted lower alkylene; R 1 is [R2-P0 M 2] H, OH, amino, substituted amino, an alkyl of from 1-6 carbon atoms, a substituted alkyl of from 1-6 carbon atoms (e.g. OH, NH2 substituted) a mononuclear aromatic radical and a substituted mononuclear aromatic radical (e.g., OH, NH 2 substituted); R 2 is R 2 or the group represented by the formula rL) ° 1 3
C —N---R.-P-OMC-N --- R-P-OM
I I II I I
20 R6 „ RVy 0M20 R6 "RVy 0M
l_ \ / Jy hvor Rg og Rg hver for sig er hydrogen, lavere alkyl med fra ca. 1-6 carbonatomer, et substitueret lavere alkyl 25 (f. eks. OH, NH2 substitueret), hydrogen, hydroxyl, ami- nogruppe, substitueret aminogruppe, et mononucleært aromatisk radikal, og et substitueret mononucleært aromatisk radikal (f. eks. OH og aminsubstitueret); R er Rg, Rg eller gruppen R2~P02M2 (R2 er som defineret i det foregåen-30 de); n er et tal fra 1 til ca. 15; Y er et tal fra ca. 1 til ca. 14, og M er som før defineret.wherein Rg and Rg are each hydrogen, lower alkyl having from ca. 1-6 carbon atoms, a substituted lower alkyl (e.g. OH, NH 2 substituted), hydrogen, hydroxyl, amino group, substituted amino group, a mononuclear aromatic radical, and a substituted mononuclear aromatic radical (e.g. OH and amine substituted); R is Rg, Rg or the group R2 ~ PO2M2 (R2 is as defined hereinbefore); n is a number from 1 to approx. 15; Y is a number from approx. 1 to approx. 14, and M is as previously defined.
Forbindelser eller formler, der kan betragtes som værende eksemplificerende for de før angivne formler, er derfor 35 som følger: nitrilo-tri(methylen-phosphonsyre) N(CH2P0gH2) DK 169709 B1 9 imino-di(methylen-phosphonsyre) NH(CH2P03H2)2 n-butyl-amino-di(methyl-phosphonsyre) C^HgN(CH2P03H2)2 5 decyl-amino-di(methyl-phosphonsyre) cioH21N^ CH2P03H2 ^ 2 trina trium-pentadecyl-amino-di-methyl-phosphat 10 C15H31N(CH2P03HNa)(CH2P03Na2) n-butyl-amino-di(ethyl-phosphonsyre) c4h9n(ch2ch2po3h2)2 15 tetranatrium-n-butyl-amino-di(methyl-phosphat) C4H9N(CH2P03Na2)2 20 triammonium-tetradecyl-amino-di(methyl-phosphat) C14H29N( CH2P03(^45 2 )CH2P03HNH4 phenyl-amino-di (methyl-phosphonsyre) CgHj-N (CI^POgHj») 2 25 4-hydroxy-phenyl-amino-di(methyl-phosphonsyre) hoc6h4n(ch2po3h2)2 30 phenyl-propyl-amino-di(methyl-phosphonsyre) C6H5(CH2)3N<CH2P03H2)2 tetranatrium-phenyl-ethyl-amino-di(methyl-phosphonsyre) C6H5 ^ CH22N^ CH2P03Na2 ^ 2 35 DK 169709 B1 10 ethylendiamin-tetra (methyl-phosphonsyre) (h2o3pch2)2n(ch2)2n(ch2po3h2)2 5 trimethylendiamin-tetra (methyl-phosphonsyre) (H203PCH2)2N(CH2)3N(CH2P03H2)2 heptamethylendiamin-tetra( methyl-phosphonsyre) 10 (H203PCH2)2N(CH2)?N(CH2P03H2)2 decamethylendiamin-tetra( methyl-phosphonsyre) 15 (H203PCH2)2N(CH2)10N(CH2P03H2)2 tetradecamethylendiamin-tetra (methyl-phosphonsyre) (H2°3PCH2)2N(CH2 >14N(CH2P03H2 > 2 20 ethylendiamin-tri (methyl-phosphonsyre) (h2o3pch2)2n(ch2)2nhch2po3h2 25 ethylendiamin-di (methyl-phosphonsyre) (h2o3pch2)2nh(ch2)2nhch2po3h2 n-hexyl-amin-di(methyl-phosphonsyre) 30 C6H13N^CH2P03H2 >2 diethylamintriamin-penta (methyl -phosphonsyre) 35 ( H203PCH2 ) 2N( CH2 ) 2N( CH2P03H2 ) - ( CH2) 2N(.CH2P03H2 ) 2 ethanolamin-di(methyl-phosphonsyre) DK 169709 B1 11 HO(CH2)2N(CH2P03H2)2 n-hexyl-amino (isopropyliden-phosphonsyre )methylphophon-5 syre C6H13N(c(ch3)2po3h2)(ch2po3h2) trihydroxymethyl, methylamin-di(methyl-phosphonsyre) 10 (hoch2)3cn(ch2po3h2)2 triethylen-tetraamin-hexa (methyl-phosphonsyre) 3.5 ( h2o3pch2 ) 2n(ch2 ) 2n( ch2po3h2 ) ( ch2 ) 2n- (CH2P03H2)(CH2)2N(CH2P03H2)2 monoethanol, diethylen-triamin-tri(methyl-phosphonsyre) 20 HOCH2CH2N( CH2P03H2) (CH2 )2NH( CH2 )2N- (C^PO^ )2 chlorethylenamin-di(methyl-phosphonsyre) cich2ch2n((ch2po(OH)2)2 25Compounds or formulas which may be considered exemplary of the previously mentioned formulas are therefore as follows: nitrilo-tri (methylene-phosphonic acid) N (CH2 PO3H2) DK 169709 B1 9 imino-di (methylene-phosphonic acid) NH (CH2PO3H2) 2 n-Butyl-amino-di (methyl-phosphonic acid) C ^HgN (CH₂PO3H₂) decyl-amino-di (methyl-phosphonic acid) cioH₂NN₂CH₂PO0H₂₂-2-triina-pentadecyl-amino-dimethyl-phosphate C15HH31NN (CH2PO3HNa) (CH2PO3Na2) n-butyl amino-di (ethyl phosphonic acid) c4h9n (ch2CH2PO3h2) 2 tetrasodium-n-butyl amino-di (methyl phosphate) C4H9N (CH2 PO3Na2) 2 triammonium amino tetradecyl di (methyl phosphate) C 14 H 29 N (CH 2 PO 3 (^ 45 2) CH 2 PO 3 HNH 4 phenylamino-di (methylphosphonic acid) CgH 2 -N (Cl 2 POgH 2) 2 4-hydroxy-phenylamino-di (methyl-phosphonic acid) hoc6h4n (ch2po3h2) 2 phenyl-propylamino-di (methyl-phosphonic acid) C6H5 (CH2) 3N <CH2PO3H2) 2 tetrasodium-phenyl-ethyl-amino-di (methyl-phosphonic acid) C6H5 ^ CH22N ^ CH2PO3Na2 ^ 2 DK 169709 B1 10 ethylenediamine tetra (methylphosphonic acid) (h2o3pch2 ) 2n (ch2) 2n (ch2po3h2) 2 trimethylenediamine tetra (methylphosphonic acid) (H2O3PCH2) 2N (CH2) 3N (CH2PO3H2) 2 heptamethylenediamine tetra (methylphosphonic acid) 10 (H2O3PCH2) 2N (CH2)? N ( CH2PO3H2) 2 decamethylenediamine tetra (methylphosphonic acid) (H2O3PCH2) 2N (CH2) 10N (CH2PO3H2) 2 tetradecamethylenediamine tetra (methylphosphonic acid) (H2 ° 3PCH2) 2N (CH2> 14N (CH2PO3H2) 2 (methylphosphonic acid) (h2o3pch2) 2n (ch2) 2nhch2po3h2 ethylenediamine di (methylphosphonic acid) (h2o3pch2) 2nh (ch2) 2nhch2po3h2 n-hexylamine di (methylphosphonic acid) C6H13N2 CH2 penta (methyl-phosphonic acid) (H 2 O 3 PO 2) 2N (CH 2) 2N (CH 2 PO 3 H 2) - (CH 2) 2 N (.CH 2 PO 3 H 2) 2 ethanolamine-di (methyl-phosphonic acid) DK 169709 B1 11 HO (CH 2) 2 N (CH 2 PO 3 H 2) 2 n -hexylamino (isopropylidene-phosphonic acid) methylphosphonic acid C6H13N (c (ch3) 2po3h2) (ch2po3h2) trihydroxymethyl, methylamine-di (methylphosphonic acid) 10 (hoch2) 3cn (ch2po3h2) 2 triethylene-tetraamine-hexa -phosphonic acid) 3.5 (h2o3pch2) 2n (ch2) 2n (ch2po 3h2) (ch2) 2n- (CH2PO3H2) (CH2) 2N (CH2PO3H2) 2 monoethanol, diethylene triamine tri (methylphosphonic acid) HOCH2CH2N (CH2PO3H2) (CH2) 2NH (CH2) 2N- (C 2 chloroethylenamine-di (methylphosphonic acid) cich2ch2n ((ch2po (OH) 2) 2
De før angivne forbindelser er angivet af illustrerende årsager, og det er ikke tilstræbt, at de skal udgøre en fuldstændig liste af de forbindelser, der kan anvendes indenfor opfindelsens rammer.The aforementioned compounds are given for illustrative reasons and it is not intended that they constitute a complete list of the compounds which may be used within the scope of the invention.
3030
De foretrukne phosphonater er de to forbindelser: A. 2-phosphonbutan-l,2,4-tricarboxylsyre og B. 1-hydroxyethan-1, 1-diphosphonsyre.The preferred phosphonates are the two compounds: A. 2-Phosphonbutane-1,2,4-tricarboxylic acid and B. 1-Hydroxyethane-1,1-diphosphonic acid.
Selv om individuelle phosphonater kan anvendes, i kombination med polymer(e), har man opnået langt bedre resul- 35 DK 169709 B1 12 tater ved at anvende en blanding af phosphonater, såsom A og B. Når de kombineres, er det i et vægtforhold A:B fra 0,5/1-4/1 og fortrinsvis fra 0,5/1-2/1, især ca. 0,67/1.Although individual phosphonates can be used, in combination with polymer (s), far better results have been obtained by using a mixture of phosphonates such as A and B. When combined, it is in a weight ratio A: B from 0.5 / 1-4 / 1 and preferably from 0.5 / 1-2 / 1, in particular approx. 0.67 / 1st
5 Udover phosphonater kan man anvende sådanne additiver som tolytriazol. Tolytriazol kan på effektiv måde reducere kobbersubstratkorrosion.In addition to phosphonates, such additives as tolytriazole can be used. Tolytriazole can effectively reduce copper substrate corrosion.
De vandopløselige, ikke tværbundne, randomiserede copoly-10 mere er beskrevet detaljeret i US patentskrift nr.The water-soluble, non-crosslinked, randomized copolymers are described in detail in U.S. Pat.
4 566 973, og specifikt er de af patenthaveren beskrevet på følgende måde:No. 4,566,973, and specifically, those described by the patent holder are as follows:
De copolymere, der er velegnet til opfindelsen, er rando-15 miserede polymere indeholdende polymeriserede enheder af en acrylsyre og substitueret acrylamid, repræsenteret ved følgende strukturformel 1: * R1 4CHr_C)-m ^h2-_;L >ert._butylThe copolymers suitable for the invention are randomized polymers containing polymerized units of an acrylic acid and substituted acrylamide, represented by the following structural formula 1: * R1 4CHr_C) -m ^ h 2 -_; L> ert._butyl
0 = C " QX 0=C - N0 = C "QX 0 = C - N
\ tert.-butyl 25 hvor m og n er tal mellem 0,1 og 700, hvorved m ligger i intervallet fra 10 til 700 og n ligger i intervallet fra 0,1 - 350, hvor der tillige foreligger molekylvægtsbegrænsninger; R og R"*· er individuelt valgt blandt hydrogen 30 og methyl; X er hydrogen, kalium, calcium, ammonium og magnesium.t-butyl 25 where m and n are numbers between 0.1 and 700, where m is in the range of 10 to 700 and n is in the range of 0.1 - 350, where there are also molecular weight constraints; R and R "are individually selected from hydrogen 30 and methyl; X is hydrogen, potassium, calcium, ammonium and magnesium.
Passende acrylsyrer til de her omhandlede formål er generelt defineret som monoumættede monocarboxylsyrer, der 35 indeholder 3-4 carbonatomer. Specifikke eksempler på sådanne syrer omfatter acryl- og methacrylsyrer, hvorved acrylsyre er særligt foretrukket.Suitable acrylic acids for the purposes of this invention are generally defined as monounsaturated monocarboxylic acids containing from 3 to 4 carbon atoms. Specific examples of such acids include acrylic and methacrylic acids, with acrylic acid being particularly preferred.
DK 169709 B1 13DK 169709 B1 13
Andre comonomere kan anvendes med en acrylsyre og et substitueret acrylamid, under forudsætning af, at sådanne yderligere comonomere ikke på skadelig måde påvirker de 5 ønskede egenskaber. Eksempler på sådanne comonomere omfatter acrylat- og methacrylat-estere, acrylamid og meth-acrylamid, acrylonitril, vinylestere, osv.Other comonomers may be used with an acrylic acid and a substituted acrylamide, provided that such additional comonomers do not adversely affect the desired properties. Examples of such comonomers include acrylate and methacrylate esters, acrylamide and methacrylamide, acrylonitrile, vinyl esters, etc.
Acryl sy reenhederne i den copolymere kan foreligge på sy-10 reform eller i en neutraliseret form, hvor hydrogenatomet i carboxylgruppen er erstattet med et alkalimetal, et jordalkalimetal eller en ammoniumkation, i afhængighed af det neutraliserende medium. Generelt kan de copolymere neutraliseres med et stærkt alkalisk materiale, såsom na-15 triumhydroxid, i hvilket tilfælde hydrogenet eller carboxylgruppen af acrylsyreenhederne vil være erstattet med natrium. Under anvendelse af et aminneutraliserende middel vil hydrogenatomet blive erstattet med en ammoniumgruppe. Anvendelige copolymere omfatter copolymere, der 20 er uneutraliserede, partielt neutraliserede og fuldstændigt neutraliserede.The acrylic acid moieties of the copolymer may be present on sieve reform or in a neutralized form, wherein the hydrogen atom in the carboxyl group is replaced by an alkali metal, an alkaline earth metal or an ammonium cation, depending on the neutralizing medium. Generally, the copolymers can be neutralized with a highly alkaline material such as sodium hydroxide, in which case the hydrogen or carboxyl group of the acrylic acid units will be replaced with sodium. Using an amine neutralizing agent, the hydrogen atom will be replaced by an ammonium group. Applicable copolymers include copolymers that are unneutralized, partially neutralized and completely neutralized.
Polymerisation af de monomere resulterer i en i det væsentlige ikke tværbundet, randomiseret copolymer, hvis 25 molekylvægt kan indstilles ved et mindre rutinepræget forsøgsarbejde. Den copolymere fremstilles fortrinsvis i et højt udbytte, der ligger mellem ca. 50 og ca. 99 vægt-% af de comonomere.Polymerization of the monomers results in a substantially non-crosslinked, randomized copolymer whose molecular weight can be adjusted by a less routine experimental work. The copolymer is preferably prepared in a high yield which is between about 50 and approx. 99% by weight of the comonomers.
30 De polymere af den før beskrevne type kan modificeres ved, at man i deres struktur inkorporerer op til 30 vægt-% af termonomer, der indeholder en ikke-ionisk eller an-ionisk polær gruppe, der fortrinsvis er valgt blandt amido, lavere alkylester og maleinsyresaltgrupper.The polymers of the type described above can be modified by incorporating in their structure up to 30% by weight of thermonomers containing a nonionic or anionic polar group preferably selected from amido, lower alkyl ester and maleinsyresaltgrupper.
Eksempler på foretrukne monomere, som kan polymeriseres til dannelse af terpolymere, er acrylamid, methyl-, eller 35 DK 169709 B1 14 ethyl-acrylat, maleinsyreanhydrid. Andre polære monomere, som kan anvendes, er f. eks. vinylacetat, acrylonitril, de forskellige vinylketoner, vinylethere og lignende. Illustrative eksempler på disse monomere er forbindelserne: 5 vinylpyrrolidon, methylvinylether, methacrylonitril, al- lylalkohol, methylmethacrylat, beta-diethylaminoethyl-me-thacrylat, vinyltrimethylacetat, methylisobutyrat, cyclo-hexylmethacrylat, vinyllaurat, vinylstearat, N-vinyl-imi-der, N-vinyl-lactamer, diethylenglycol-dimethacrylat, di-10 allylmaleat, allylmethacrylat, diallyl-phthalat, diallyl- adipat osv.Examples of preferred monomers which can be polymerized to form terpolymers are acrylamide, methyl, or ethyl acrylate, maleic anhydride. Other polar monomers which may be used are, for example, vinyl acetate, acrylonitrile, the various vinyl ketones, vinyl ethers and the like. Illustrative examples of these monomers are the compounds: vinyl pyrrolidone, methyl vinyl ether, methacrylonitrile, alkyl alcohol, methyl methacrylate, beta-diethylaminoethyl methacrylate, vinyl trimethyl acetate, methyl isobutyrate, cyclohexyl methacrylate, vinyl laurate, vinyl laurate, vinyl laurate, vinyl laurate, vinyl laurate vinyl lactamer, diethylene glycol dimethacrylate, di-allyl maleate, allyl methacrylate, diallyl phthalate, diallyl adipate, etc.
De dannede polymere skal have en gennemsnitlig molekylvægt efter vægt i intervallet fra 1000 til 50000, og for-15 trinsvis 2000 til 30000, bestemt ved vandig gelpermea-tionschromatografi under anvendelse af polystyren med kendt molekylvægt som referencemateriale.The polymers formed must have an average molecular weight by weight in the range of 1000 to 50,000, and preferably 2000 to 30000, determined by aqueous gel permeation chromatography using polystyrene of known molecular weight as a reference material.
Syretallene af de dannede copolymere, bestemt ved en kon-20 ventionel titrering med KOH, er fra 310 til 740, svarende til en vægtfraktion på fra 40 til 95 vægt-% af monomerenheder, der har C00H grupper. De foretrukne polymere har mere end 50 vægt-% frie carboxylgrupper og et syretal mellem 390 og 700.The acid numbers of the copolymers formed, determined by conventional titration with KOH, are from 310 to 740, corresponding to a weight fraction of from 40 to 95% by weight of monomer units having C00H groups. The preferred polymers have more than 50 wt% free carboxyl groups and an acid number between 390 and 700.
2525
Foretrukne materialer er beskrevet i tabel A i det følgende som polymerblandinger nr. 1-12.Preferred materials are described in Table A below as polymer blends Nos. 1-12.
30 35 DK 169709 B1 1530 35 DK 169709 B1 15
Tabel ATable A
Polymere materialer 5 PolymerPolymeric Materials 5 Polymer
Materiale nr. M.W. Materiale, mol-% 1 9300 AA/t-BAm 88:12 2 12000 3 17700 10 4 25900 5 8900 AA/EA/t-BAm 86:8:6 6 9400 AA/Am/t-BAm 84:11:6 15 -------------------------------------------------------- 7 8200 AA/MAA/t-BAm 68:19:13 8 13300* 9 14300* " 10 15700* 20 11 15600 12 23000Material No. M.W. Material, mole% 1 9300 AA / t-BAm 88:12 2 12000 3 17700 10 4 25900 5 8900 AA / EA / t-BAm 86: 8: 6 6 9400 AA / Am / t-BAm 84: 11: 6 15 ------------------------------------------------- ------- 7 8200 AA / MAA / t-BAm 68:19:13 8 13300 * 9 14300 * "10 15700 * 20 11 15600 12 23000
Gennemsnitlig molekylvægt efter vægt, dvs. M.W. eller Mw· 25 * Vandig M evalueret på basis af værdien af GPC underAverage molecular weight by weight, ie. W., or Mw · 25 * Aqueous M evaluated based on the value of GPC below
WW
anvendelse af THF som eluent.using THF as eluent.
Polymerblandinger nr. 1-4 er uneutraliserede copolymere 30 af acrylsyre og t-butyl-acrylamid (t-BAm). Polymerblanding nr. 5, polymerblanding nr. 6 og polymerblanding nr.Polymer blends # 1-4 are unneutralized copolymers 30 of acrylic acid and t-butyl acrylamide (t-BAm). Polymer Blend # 5, Polymer Blend # 6 and Polymer Blend #
7 er terpolymere, der indeholder de yderligere mer-enhe-der henholdsvis ethylacrylat (EA), acrylamid (Am) og methacrylsyre (MAA).7 are terpolymers containing the additional mer units ethyl acetate (EA), acrylamide (Am) and methacrylic acid (MAA), respectively.
Et kendetegnende træk ved alle disse polymere er t-butyl-acrylamid-enheden. Denne sterisk hindrede, hydrophobe al- 35 DK 169709 B1 16 kylamidgruppe udviser udmærket resistens over for hydrolyse og enheden synes at meddele exceptionelle egenskaber.A distinguishing feature of all these polymers is the t-butyl acrylamide moiety. This sterically hindered hydrophobic alkylamide group exhibits excellent resistance to hydrolysis and the unit appears to confer exceptional properties.
5 De copolymere, der består af acrylsyre og t-butyl-acrylamid, indeholder mellem 50 og 90 vægt-% acrylsyre og fra 10-50 vægt-% t-butyl-acrylamid. Fortrinsvis foreligger acrylsyren i en vægt-%, der ligger fra 70-90, hvorved t-butyl-acrylamidet er til stede i en mængde mellem 10-30.The copolymers consisting of acrylic acid and t-butyl acrylamide contain between 50 and 90 wt% acrylic acid and from 10-50 wt% t-butyl acrylamide. Preferably, the acrylic acid is present in a weight percent ranging from 70-90, whereby the t-butyl acrylamide is present in an amount between 10-30.
10 I det mest foretrukne tilfælde foreligger acrylsyren i en vægt-%, der ligger mellem 80-90, idet t-butyl-acrylamidet er til stede i en mængde mellem 10-20.In the most preferred case, the acrylic acid is present in a weight% ranging from 80-90, with the t-butyl acrylamide present in an amount between 10-20.
De terpolymere ligger inden for følgende intervaller hvad 15 angår vægt-%: a) acrylsyre 40-90, især 40-80 og i særdeleshed 60-80 b) methacrylsyre 5-30, især 10-30 og i særdeleshed 10-20 20 c) t-butyl-acrylamid 5-50, især 10-30 og i særdeleshed 10-20The terpolymers are within the following ranges of 15% by weight: a) acrylic acid 40-90, especially 40-80 and especially 60-80 b) methacrylic acid 5-30, especially 10-30 and in particular 10-20 20 c t-butyl acrylamide 5-50, in particular 10-30 and in particular 10-20
Det vandige system doseres på basis af aktive bestanddele, således at der på substratet på vægtbasis tilveje-25 bringes fra mellem 5-50 ppm, fortrinsvis 8-40 ppm, især 15-30 ppm af blandingerne I og II, som tidligere beskre vet.The aqueous system is dosed on the basis of active ingredients so that on the weight basis the substrate is obtained from between 5-50 ppm, preferably 8-40 ppm, especially 15-30 ppm of mixtures I and II, as previously described.
Når blandingerne først tilsættes, er det fordelagtigt, 30 hvis de doseres på den høje side for at kontrollere korrosionen og for at begynde dannelsen af beskyttende film. Efter omkring en uges forløb kan doserne reduceres, indtil der etableres en optimal vedligeholdelsesdosis.When the mixtures are first added, it is advantageous if dosed on the high side to control the corrosion and to begin the formation of protective films. After about a week, the doses can be reduced until an optimal maintenance dose is established.
35 De systemer, der behandles, er industrielle recirkuleren-de vandmasser eller kølevand, der løber én gang igennem, som enten på grund af deres naturlige sammensætning eller DK 169709 B1 17 ved pH-indstilling har et pH på mindst 8. Fortrinsvis ligger pH af systemerne indenfor intervallet 8-9,5, og oftest indenfor intervallet 8,5-9,2. Disse systemer er karakteriseret som indeholdende mindst 10 ppm calciumion 5 og antages at være korroderende overfor ferrometaller samt ikke-ferro-metaller, med hvilke de kommer i kontakt.The systems being treated are once-through-flow industrial recycled water or cooling water which, either due to their natural composition or at pH adjustment, has a pH of at least 8. Preferably, the pH of systems within the range of 8-9.5, and most often within the range of 8.5-9.2. These systems are characterized as containing at least 10 ppm calcium ion 5 and are believed to be corrosive to ferrous metals as well as non-ferrous metals with which they come into contact.
Det følgende eksempel er en repræsentativ formulering, der anvendes i dette program.The following example is a representative wording used in this program.
1010
Eksempel 1Example 1
Til en beholder af glas eller rustfrit stål tilføres der 14 g blødt vand. Under omrøring tilsætter man konsekutivt 15 vandige opløsninger af følgende materialer: 7 g 1-hydroxyethan-l,1-diphosphonsyre (60 vægt-%) 12 g 2-phosphonobutan-l,2,4-tricarboxylsyre (50 vægt-%) 20 15,3 g acrylsyre/t-butylacrylamid-copolymer (49 vægt-%).To a glass or stainless steel container is added 14 g of soft water. With stirring, 15 aqueous solutions of the following materials are consecutively added: 7 g of 1-hydroxyethane-1,1-diphosphonic acid (60% by weight) 12 g of 2-phosphonobutane-1,2,4-tricarboxylic acid (50% by weight) , 3 g of acrylic acid / t-butyl acrylamide copolymer (49% by weight).
Blandingen blev afkølet i et isbad og derpå gjort basisk ved langsom tilsætning af ca. 22 g vandigt natriumhydro-25 xid (50 vægt-%) til den under kraftig omrøring stående opløsning. Under tilsætningen af basen blev opløsningens temperatur holdt under 54 °C. pH blev indstillet til 13 med 4,7 g af en 50 vægt-% af en opløsning af natriumto-lyltriazol. Slutteligt tilsatte man blødgjort vand i en 30 mængde, der var tilstrækkelig til at frembringe 100 g produkt. Kølebadet blev fjernet, og opløsningen blev holdt under omrøring, indtil temperaturen var lig omgivelsernes temperatur.The mixture was cooled in an ice bath and then basified by the slow addition of ca. 22 g aqueous sodium hydroxide (50 wt%) to the solution with vigorous stirring. During the addition of the base, the temperature of the solution was kept below 54 ° C. The pH was adjusted to 13 with 4.7 g of a 50 wt% of a solution of sodium tolyl triazole. Finally, softened water was added in a quantity sufficient to produce 100 g of product. The cooling bath was removed and the solution kept under stirring until the temperature was equal to ambient temperature.
35 Ændringer i formuleringen foretages let ved simpel modifikation af den i det foregående beskrevne metode. F. eks. vil en reduktion af mængden af polymer og natriumhy DK 169709 B1 18 droxid, efterfulgt af forøgelse af den sluttelige mængde af tilsat vand, frembringe en formulering, der indeholder lavere aktive polymerbestanddele. Som et alternativ kan den polymere og korrosionsinhibitorerne tilføres separat, 5Changes to the formulation are easily made by simple modification of the method described above. For example, a reduction in the amount of polymer and sodium hydroxide, followed by increasing the final amount of added water, will produce a formulation containing lower active polymeric constituents. Alternatively, the polymeric and corrosion inhibitors may be added separately, 5
Ved laboratorieforsøg udtrykkes hårdhedsdannende kationer M og alkalinitet som CaCO^ eller cycler af koncentration.In laboratory experiments, hardness-forming cations M and alkalinity are expressed as CaCO 3 or cycles of concentration.
Fe+n er opført som Fe, og inhibitorer (monomere og polymere) er opført som aktive stoffer. I analyser af udfæld-10 ninger af varmevekslere er alle komponenter opført som vægt-% af det kemiske grundstof eller af syreformen af forbindelsen.Fe + n is listed as Fe, and inhibitors (monomers and polymers) are listed as active substances. In analyzes of precipitates of heat exchangers, all components are listed as weight percent of the chemical element or of the acid form of the compound.
Man gjorde brug af en som standard tjenende "bæger"-prøve 15 til at evaluere egenskaberne af phosphonat-inhibitorer .A standard "beaker" sample 15 was used to evaluate the properties of phosphonate inhibitors.
(tabel B). Man anvendte calcium- og inhibitor-stamopløsninger fra inhiberingsprøven med calciumphosphat. Desuden fremstilledes stamopløsninger (1000 ppm aktive stoffer) af Bayer PBS-AM og Dequest 2010 Dequest-2010, fremstillet 20 af Monsanto Company, St. Louis, Missouri, beskrives som hydroxy-ethyliden-1, 1-diphosphonsyre (HEDP) (jfr. US patentskrift nr. 3 959 168). PBS-AM er et varemærke fra Bayer for 2-phosphonobutan-l,2,4-tricarboxylsyre. Når man begynder prøven, tilfører man destilleret vand (400 ml) 25 til de med kapper forsynede bægre, der blev holdt på 60 τ 2 °C. Stamopløsningerne blev tilsat for at opnå 360 ppm • 2(Table B). Calcium and inhibitor stock solutions from the calcium phosphate inhibition sample were used. In addition, stock solutions (1000 ppm of active substances) were prepared by Bayer PBS-AM and Dequest 2010 Dequest-2010, manufactured by Monsanto Company, St. Louis, Missouri, is described as hydroxyethylidene-1,1-diphosphonic acid (HEDP) (cf. U.S. Patent No. 3,959,168). PBS-AM is a trademark of Bayer for 2-phosphonobutane-1,2,4-tricarboxylic acid. When starting the sample, add distilled water (400 ml) 25 to the sheathed cups held at 60 τ 2 ° C. The stock solutions were added to obtain 360 ppm • 2
Ca' , 10 ppm inhibitor, 5,6 ppm Dequest og 8 ppm PBS-AM i det sluttelige forsøgsvolumen på 500 ml. Dernæst blev pH indstillet på 9,2 under anvendelse af vandigt natriumhy-30 droxid.Ca ', 10 ppm inhibitor, 5.6 ppm Dequest and 8 ppm PBS-AM in the final 500 ml test volume. Next, the pH was adjusted to 9.2 using aqueous sodium hydroxide.
pH-værdierne i forsøgsprøverne blev manuelt indstillet på 15 minutters intervaller under den første time og derpå med intervaller af 1 time. En varighed af prøven på fire 35 timer var tilstrækkelig til, at disse bundfældningsreak tioner kunne stabilisere. Slutteligt blev en del af hver prøveopløsning ført gennem et Millipore filter af typen DK 169709 B1 19 celluloseacetat/nitrat (type HA, 0,45 um). Både filtrerede og ikke filtrerede alikvoter blev spektrophotometrisk analyseret for totalt phosphatindhold. For at studere bivirkninger ved partiklerne blev en yderligere prøve ført 5 gennem et 0,10 um Millipore filter (type VC). Den procen-tiske inhibering blev bestemt under anvendelse af den følgende formel: [filtreret - kontrol] 10 % inhibering ---------------------------X 100 [ufiltreret - kontrol] 15 20 25 30 35 DK 169709 B1 20The pH values in the test samples were manually set at 15 minute intervals during the first hour and then at 1 hour intervals. A duration of the sample of four 35 hours was sufficient to stabilize these precipitation reactions. Finally, part of each sample solution was passed through a Millipore filter of type DK 169709 B1 19 cellulose acetate / nitrate (type HA, 0.45 µm). Both filtered and non-filtered aliquots were spectrophotometrically analyzed for total phosphate content. To study the side effects of the particles, a further sample was passed through a 0.10 µm Millipore filter (type VC). The percent inhibition was determined using the following formula: [filtered - control] 10% inhibition --------------------------- X 100 [unfiltered - control] 15 20 25 30 35 DK 169709 B1 20
Tabel 8Table 8
Calciumphosphonat-inhibering 5 10 ppm polymer-aktive stoffer 5,6 ppm Dequest 2010 og 8 ppm Bayer PBS-AM (som aktive stoffer) 360 pm Ca (som CaCOg) 60 °C/pH 9,2/4 h.Calcium phosphonate inhibition 5 10 ppm polymer active substances 5.6 ppm Dequest 2010 and 8 ppm Bayer PBS-AM (as active substances) 360 pm Ca (as CaCOg) 60 ° C / pH 9.2 / 4 h.
10 % Inhibering10% inhibition
Polymer ...filterstørrelse (tint)...Polymer ... filter size (thawed) ...
forbindelse nr. (M.W. H^O) 0,45_0,10_ 1 (9300) 82% 26 15 5 (8900) 74 24 6 (9400) 8 13 11 (15600) 98 58Compound No. (M.W. H 2 O) 0.45_0.10_ 1 (9300) 82% 26 15 5 (8900) 74 24 6 (9400) 8 13 11 (15600) 98 58
Versa TL-4 (19000) 95 26 20Versa TL-4 (19000) 95 26 20
Ved inhiberingsprøverne med calciumphosphonat undersøgte man egenskaberne af den polymere versus partikelstørrelsen af bundfaldet, og resultaterne er repræsenteret i tabel B.In the calcium phosphonate inhibition tests, the properties of the polymer versus particle size of the precipitate were investigated and the results are represented in Table B.
25 "Inhiberings"-processen med calciumphosphonat involverer, at man minimerer partikelvækst. Bibeholdelse af kedelstenspartikler på en meget ringe partikelstørrelse og masse kan i sidste instans vise sig at være en kritisk 30 faktor ved bestemmelse af polymeregenskaberne. Ved at anvende filtre med gennemsnitlige porestørrelser af 0,10 og 0,45 um kunne man let iagttage forskelle i polymeregenskaberne. Polymerblanding nr. 11 (molekylvægt = 15.600) frembragte som helhed betragtet de bedste egenskaber, og 35 den var den eneste polymer, der udviste god inhibering, når man anvendte et 0,10 wm filter. Versa TL-4 (den lavmolekylære copolymer af sulfoneret styren og maleinsyre) DK 169709 B1 21 og polymerblanding nr. 1 og 5 udviste udmærket inhibering (0,45 um filter), men egenskaberne forringedes hurtigt, når størrelsen af filterporerne blev reduceret til 0,10 um. Især udviste polymerblanding nr. 11 som helhed be-5 tragtet de bedste egenskaber, både i prøverne af typen "bench-top" og i PCT-prøverne.The "calcium phosphonate" inhibition "process involves minimizing particle growth. Retention of scale particles at a very small particle size and mass may ultimately prove to be a critical factor in determining polymer properties. By using filters with average pore sizes of 0.10 and 0.45 µm, differences in polymer properties could be easily observed. Polymer blend # 11 (molecular weight = 15,600), as a whole, considered the best properties and was the only polymer to exhibit good inhibition when using a 0.10 wm filter. Versa TL-4 (the low molecular weight copolymer of sulfonated styrene and maleic acid) DK 169709 B1 21 and polymer blend Nos. 1 and 5 showed excellent inhibition (0.45 µm filter), but the properties deteriorated rapidly when the size of the filter pores was reduced to 0. 10 pm In particular, polymer blend # 11 as a whole showed the best properties, both in the "bench-top" and PCT samples.
Køletårnsprøven af pilottypen er en dynamisk prøve, der simulerer mange træk, der foreligger i et industrielt sy-10 stem med recirkulerende kølevand. Den generelle prøvemetode er beskrevet i artiklen "Small-Scale Short-Term Methods of Evaluating Cooling Water Treatments...Are They Worthwhile?", af D. T. Reed og R. Nass, referat af det 36. årlige møde af INTERNATIONAL WATER CONFERENCE, 15 Pittsburgh, Pennsylvania, November 4-6, 1975.The pilot-type cooling tower test is a dynamic test that simulates many features of an industrial system with recirculating cooling water. The general test method is described in the article "Small-Scale Short-Term Methods of Evaluating Cooling Water Treatments ... Are They Worthwhile?", By DT Reed and R. Nass, Minutes of the 36th Annual Meeting of the INTERNATIONAL WATER CONFERENCE, 15 Pittsburgh, Pennsylvania, November 4-6, 1975.
De generelle driftsbetingelser er sammenstillet i tabel C.The general operating conditions are summarized in Table C.
20 25 30 35 DK 169709 B1 2220 25 30 35 DK 169709 B1 22
Tabel CTable C
Driftsbetingelser i køletårn af pilot plant størrelse 5 Rør # Metal*/Varmebelastning (Btu/ft2-h) 8 MS/15,000 (top) 7 SS/15,000 6 MS/12,400 5 Adm/5,000 10 4 MS/5,000 3 SS/12,400 2 Adm/12,400 1 SS/12,400 (bund) 15 Suppleringsvand: Synthetic #31 Ønskede Cycler: 4Operating conditions in pilot plant cooling tower size 5 Pipes # Metal * / Heat load (Btu / ft2-h) 8 MS / 15,000 (top) 7 SS / 15,000 6 MS / 12,400 5 Adm / 5,000 10 4 MS / 5,000 3 SS / 12,400 2 Adm / 12,400 1 SS / 12,400 (bottom) 15 Supply water: Synthetic # 31 Desired Cycles: 4
Basinvolumen/temp.2 ‘50 1 /52 °CBasin volume / temp.2 '50 1/52 ° C
Holdetidsindex 24 hHold time index 24 h
Strømningshastighed 7,56 1/min 20 pH 9,2Flow rate 7.56 l / min pH 9.2
Produkt - højt niveau 200 ppmProduct - high level 200 ppm
Produkt - vedligeholdelse 100 ppmProduct maintenance 100 ppm
Varighed af prøve 14 dage 25 *MS = blødt stålDuration of sample 14 days 25 * MS = soft steel
Adm = Specialmessing SS = 306 rustfrit stålAdm = Special brass SS = 306 stainless steel
Synthetic #3 indeholder et totalt ionindhold af 90 +2 +2 — 30 ppm Ca , 50 ppm Mg , 90 ppm Cl , 50 ppm sulfat, 110 ppm Na+ og 110-120 ppm ”M" alkalinitet (som CaCO^)· 2Synthetic # 3 contains a total ion content of 90 + 2 + 2 - 30 ppm Ca, 50 ppm Mg, 90 ppm Cl, 50 ppm sulfate, 110 ppm Na + and 110-120 ppm "M" alkalinity (as CaCO 2) · 2
Returvand er 5,6 eC højere 35 Polymerblandingerne nr. 1, 3, 5, 6, 7 og 11, som beskrevet i tabel D, blev fremstillet i henhold til eksempel 1 og blev anvendt til direkte erstatning af VTL-4 i standardformuleringen ved højt pH. Stabilitetsprøvning i længere tid (49 °C/pH 13) for disse formuleringer udført i DK 169709 B1 23 henhold til metoden i eksempel 1, men indeholdende poly-merblandingeme nr. 1, 6 eller 11, afslørede, at der ikke forekom nogen hydrolyse af den polymere over en 3 måneders periode. PCT udfældning/korrosion hastighederne er 5 sammenstillet i den følgende tabel D.Return water is 5.6 eC higher. Polymer blends Nos. 1, 3, 5, 6, 7 and 11, as described in Table D, were prepared according to Example 1 and were used to directly replace VTL-4 in the standard high formulation formulation. pH. Prolonged stability testing (49 ° C / pH 13) for these formulations carried out in DK 169709 B1 23 according to the method of Example 1, but containing polymer blends # 1, 6 or 11, revealed that no hydrolysis of the polymer over a 3 month period. The PCT precipitation / corrosion rates are summarized in the following Table D.
10 15 20 25 30 35 24 DK 169709 B1 0Η*·0Η0Η00 < O V V V S k10 15 20 25 30 35 24 DK 169709 B1 0Η * · 0Η0Η00 <O V V V S k
CQ ΙΟ IOOOOOOCQ ΙΟ IOOOOOO
03 'W' '--- *>--' N--' Se" 'W'03 'W' '--- *> -' N-- 'See "' W"
M^l* O H 00 -ί O HM ^ l * O H 00 -ί O H
R * *.R * *.
•to 10 H CO IO H lO H in• to 10 H CO IO H 10 H in
\ H t—1 I\ H t— 1 I
R g /~S /“SR g / ~ S / “S
©. i ^in^inoinin^^ R νθ<Ψ000030ΝΟΝ tli g kss*»*.«.*.·.©. i ^ in ^ inoinin ^^ R νθ <Ψ000030ΝΟΝ tli g kss * »*.«. *. ·.
0) >ίΌΟΟΟΟΟΟΟΟΟ C Ol s*-/ "w/ "w" W N·^ "ri g0)> ίΌΟΟΟΟΟΟΟΟΟ C Ol s * - / "w /" w "W N · ^" ri g
H w in H C^HH w in H C ^ H
03 V V N V K V.03 V V N V K V.
X C OOHOOOOOOOOOOOOHX C OOHOOOOOOOOOOOOH
0) 0 NSCOISC^OOCOC^C"0) 0 NSCOISC ^ OOCOC ^ C "
> H <N> H <N
Ό 03Ό 03
3 O >*N. *»S, /—N y-V K m ^ 4-> J3 O> * N. * »S, / —N y-V K m ^ 4-> J
0) R coætoaHnnoico totORto ε r *»»*>***«» -Por0) R coætoaHnnoico totORto ε r * »» *> *** «» -Por
R OCQ CONHNCOHHNN ,, .¾ t-> <DR OCQ CONHNCOHHNN ,, .¾ t-> <D
(0 & ΣΙ s—' '—-* ^ v" »—« ^ <w» v H. IT1 hi p| > R n tn ε q ·δ S * 'S 43 O) ti é Η ε S <D <D O)(0 & ΣΙ s— '' —- * ^ v "» - «^ <w» v H. IT1 hi p |> R n tn ε q · δ S * 'S 43 O) ti é Η ε S <D <DO)
β g* C > Rβ g * C> R
Λ 0) ^ I R T3 OΛ 0) ^ I R T3 O
tO 03 σ S <D ·©· -n ε· h to r p c ©.tO 03 σ S <D · © · -n ε · h to r p c ©.
Φ *α B 03 Λ 'O \ 03 R X s C »osliNt^chNM'incsc^ t; <d & τ3 Η ε I ^fCO’iC^aHMN g H 0) Λ w * C 3 > R Q) ,0 B) C *0 CJ 0) *H C ε 0) § 03Φ * α B 03 Λ 'O \ 03 R X s C »osliNt ^ chNM'incsc ^ t; <d & τ3 Η ε I ^ fCO'iC ^ aHMN g H 0) Λ w * C 3> R Q), 0 B) C * 0 CJ 0) * H C ε 0) § 03
-rlOOOONlOvOOCOHIS RCH-rlOOOONlOvOOCOHIS RCH
H C < H Η N H _· °<0 .(¾ Q)H C <H Η N H _ · ° <0. (¾ Q)
*0 δ 01 R C* 0 δ 01 R C
R H g C B C - a) æ > to 3 to p m ωοίθνοΗθ>Ηθ^ a ό to Oosi^pc^coisoinNinin p ό Η »R H g C B C - a) æ> to 3 to p m ωοίθνοΗθ> Ηθ ^ a O to Oosi ^ pc ^ coisoinNinin p ό Η »
•P D 21 η h R (0 "j C• P D 21 η h R (0 ”j C
H ·©. > 2 0)H · ©. > 2 0)
3 Ή £ Λ +J3 Ή £ Λ + J
CO g . 03CO g. 03
O (!) C B HO (!) C B H
£ ^ ^ * C O ,R <D£ ^ ^ * C O, R <D
* inninininin* c Η ^ Ό R* inninininin * c Η ^ Ό R
^ Q) p Φ 0) E> t> C". [S (N IN LD D)^©Ai > R >—'W'w'WWWW 3S ©·^ Q) p Φ 0) E> t> C ". [S (N IN LD D) ^ © Ai> R> - 'W'w'WWWW 3S © ·
0> s, Ό p R R0> s, Ό p R R
gH00W«D^HH ? Q) 0) o OigH00W «D ^ HH? Q) 0) o Oi
— >1 HH 5 R 03 P-> 1 HH 5 R 03 P
R H 2 H 03 OR H 2 H 03 O
0) O R -P 0) (1) p <w afi= = = = = s c O) p ~ c c R ε <w O C Di in (D fl) -H (D (00) O R -P 0) (1) p <w afi = = = = = s c O) p ~ c c R ε <w O C Di in (D fl) -H (D (0
P O) a *· > D -P RP O) a * ·> D -P R
03 O) *H C^-Θ-ΦΡ p03 O) * H C ^ -Θ-ΦΡ p
CO w R . Λ μ HCO w R. Λ µ H
<D -H C au®* C<D -H C au® * C
> (0 Η ° > Φ 03 h i η i o ©· · ε p £)= = = = = = ►£ R CO P C R O)> (0 Η °> Φ 03 h i η i o © · · ε p £) = = = = = = ► £ R CO P C R O)
R * HR Eh P CO ft <D 0) CR * HR Eh P CO ft <D 0) C
<D (0 O 0) C ·> R C<D (0 O 0) C ·> R C
ε r ε <o o -oo <h m c <u s* ε -p >t 03«·^(0(0ροε r ε <o o -oo <h m c <u s * ε -p> t 03 «· ^ (0 (0ρο
Η & C H RΗ & C H R
o a o o o) * a *j\ x a > * * DK 169709 B1 25o a o o o) * a * j \ x a> * * DK 169709 B1 25
Det har i visse tilfælde vist sig anbefalelsesværdigt at tilsætte små mængder af tolytriazol.In some cases it has been recommended to add small amounts of tolytriazole.
Tolytriazol er forklaret i Hackh’s Chemical Dictionary, 5 fjerde udgave, side 91 (jfr. benzotriazol) og anvendes som korrosionsinhibitor for overflader af kobber og kobberlegeringer i kontakt med vand; når det anvendes, bruges det i systemet i en dosis mellem 1 og 20 ppm på vægtbasis.Tolytriazole is explained in Hackh's Chemical Dictionary, 5th Edition, page 91 (cf. benzotriazole) and is used as a corrosion inhibitor for copper and copper alloy surfaces in contact with water; when used, it is used in the system at a dose between 1 and 20 ppm by weight.
10 15 20 25 30 3510 15 20 25 30 35
Claims (7)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US84441586A | 1986-03-26 | 1986-03-26 | |
US84441586 | 1986-03-26 |
Publications (3)
Publication Number | Publication Date |
---|---|
DK150787D0 DK150787D0 (en) | 1987-03-25 |
DK150787A DK150787A (en) | 1987-09-27 |
DK169709B1 true DK169709B1 (en) | 1995-01-16 |
Family
ID=25292665
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK150787A DK169709B1 (en) | 1986-03-26 | 1987-03-25 | Corrosion Inhibition Method |
Country Status (16)
Country | Link |
---|---|
EP (1) | EP0238728B1 (en) |
JP (1) | JPS62270786A (en) |
CN (1) | CN1019989C (en) |
AT (1) | ATE56051T1 (en) |
AU (1) | AU593082B2 (en) |
BR (1) | BR8701331A (en) |
CA (1) | CA1329474C (en) |
DE (1) | DE3673809D1 (en) |
DK (1) | DK169709B1 (en) |
ES (1) | ES2016796B3 (en) |
FI (1) | FI871242A (en) |
GR (1) | GR3001105T3 (en) |
MX (1) | MX173411B (en) |
PT (1) | PT84551B (en) |
TR (1) | TR24741A (en) |
ZA (1) | ZA872236B (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4717542A (en) * | 1987-01-23 | 1988-01-05 | W. R. Grace & Co. | Inhibiting corrosion of iron base metals |
WO1989007633A1 (en) * | 1988-02-18 | 1989-08-24 | John Kenneth Bethune | Absorbent polymer compositions |
CN1034738C (en) * | 1993-03-27 | 1997-04-30 | 云浮硫铁矿企业集团公司 | A protectant composition |
GB9505675D0 (en) * | 1995-03-21 | 1995-05-10 | Diversey Corp | Cleaning compositions |
CA2599940C (en) * | 2005-03-04 | 2011-11-29 | The Procter & Gamble Company | Automatic dishwashing composition with corrosion inhibitors |
CN101368091B (en) * | 2007-08-16 | 2012-01-11 | 中国石油天然气集团公司 | Oil well cement retarder |
CN101560022B (en) * | 2009-05-26 | 2011-05-11 | 西安协力动力科技有限公司 | Compound corrosion and scale inhibitor |
US11085118B2 (en) | 2016-04-14 | 2021-08-10 | Nch Corporation | Composition and method for inhibiting corrosion and scale |
US10351453B2 (en) | 2016-04-14 | 2019-07-16 | Nch Corporation | Composition and method for inhibiting corrosion |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1208827A (en) * | 1968-02-23 | 1970-10-14 | Grace W R & Co | Composition and process for inhibiting scaling and/or corrosion in cooling water systems and for stabilizing phosphate solutions |
DE2333353C2 (en) * | 1973-06-30 | 1983-05-19 | Bayer Ag, 5090 Leverkusen | Process for preventing corrosion in water-bearing systems and anti-corrosion agents for carrying out the process |
US4317744A (en) * | 1979-04-25 | 1982-03-02 | Drew Chemical Corporation | Corrosion inhibitor |
GB2124607B (en) * | 1982-07-16 | 1986-02-05 | Katayama Chemical Works Co | Scale-inhibiting agent |
US4566973A (en) * | 1984-08-06 | 1986-01-28 | The B. F. Goodrich Company | Scale inhibition in water systems |
GB2168359B (en) * | 1984-11-08 | 1988-05-05 | Grace W R & Co | A method of inhibiting corrosion in aqueous systems |
US4650591A (en) * | 1985-08-29 | 1987-03-17 | Calgon Corporation | Acrylic acid/2-acrylamido-2-methylpropylsulfonic acid/2-acrylamido-2-methylpropyl phosphonic acid polymers as scale and corrosion inhibitors |
US4752443A (en) * | 1986-05-09 | 1988-06-21 | Nalco Chemical Company | Cooling water corrosion inhibition method |
-
1986
- 1986-12-30 ES ES86118127T patent/ES2016796B3/en not_active Expired - Lifetime
- 1986-12-30 EP EP86118127A patent/EP0238728B1/en not_active Expired - Lifetime
- 1986-12-30 DE DE8686118127T patent/DE3673809D1/en not_active Expired - Fee Related
- 1986-12-30 AT AT86118127T patent/ATE56051T1/en not_active IP Right Cessation
-
1987
- 1987-02-10 CA CA000529357A patent/CA1329474C/en not_active Expired - Fee Related
- 1987-03-20 JP JP62067764A patent/JPS62270786A/en active Granted
- 1987-03-20 FI FI871242A patent/FI871242A/en not_active Application Discontinuation
- 1987-03-24 BR BR8701331A patent/BR8701331A/en not_active IP Right Cessation
- 1987-03-24 MX MX005678A patent/MX173411B/en unknown
- 1987-03-24 PT PT84551A patent/PT84551B/en not_active IP Right Cessation
- 1987-03-24 TR TR87/0194A patent/TR24741A/en unknown
- 1987-03-25 DK DK150787A patent/DK169709B1/en not_active IP Right Cessation
- 1987-03-25 AU AU70632/87A patent/AU593082B2/en not_active Ceased
- 1987-03-25 CN CN87102313A patent/CN1019989C/en not_active Expired - Fee Related
- 1987-03-26 ZA ZA872236A patent/ZA872236B/en unknown
-
1990
- 1990-11-26 GR GR90400963T patent/GR3001105T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
DK150787D0 (en) | 1987-03-25 |
JPH0146593B2 (en) | 1989-10-09 |
CN1019989C (en) | 1993-03-03 |
EP0238728A1 (en) | 1987-09-30 |
ES2016796B3 (en) | 1990-12-01 |
EP0238728B1 (en) | 1990-08-29 |
TR24741A (en) | 1992-03-06 |
DE3673809D1 (en) | 1990-10-04 |
PT84551B (en) | 1989-11-10 |
JPS62270786A (en) | 1987-11-25 |
MX5678A (en) | 1993-09-01 |
MX173411B (en) | 1994-03-02 |
GR3001105T3 (en) | 1992-05-12 |
AU593082B2 (en) | 1990-02-01 |
AU7063287A (en) | 1987-10-01 |
FI871242A (en) | 1987-09-27 |
FI871242A0 (en) | 1987-03-20 |
ZA872236B (en) | 1987-11-25 |
DK150787A (en) | 1987-09-27 |
CA1329474C (en) | 1994-05-17 |
PT84551A (en) | 1987-04-01 |
BR8701331A (en) | 1988-01-05 |
CN87102313A (en) | 1988-02-24 |
ATE56051T1 (en) | 1990-09-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DK171302B1 (en) | Process for corrosion inhibition in aqueous systems, in particular cooling water systems | |
US4929425A (en) | Cooling water corrosion inhibition method | |
US4923634A (en) | Cooling water corrosion inhibition method | |
US4744949A (en) | Method for preventing corrosion in aqueous systems | |
US4913822A (en) | Method for control of scale and inhibition of corrosion in cooling water systems | |
CA1291635C (en) | Composition of corrosion inhibitors for cooling water systems using chemically modified acrylamide or methacrylamide polymers | |
US6641754B2 (en) | Method for controlling scale formation and deposition in aqueous systems | |
US5282976A (en) | Terpolymer useful as a scale inhibitor | |
DK169709B1 (en) | Corrosion Inhibition Method | |
EP0077187B1 (en) | Method of inhibiting corrosion and controlling deposition in an aqueous medium | |
CA1114978A (en) | Sludge conditioning composition for scale inhibition in water | |
US7405263B2 (en) | Polymer for water treatment | |
MXPA06009128A (en) | Desalination scale inhibitors | |
US4904413A (en) | Cooling water corrosion control method and composition | |
CA1309854C (en) | Inhibiting corrosion of iron base metals | |
CA2015718A1 (en) | Inhibition of corrosion in aqueous systems | |
CA1243917A (en) | Process and agent for the prevention of tartrate deposits | |
GB2087862A (en) | Process for dispersing particulate material in aqueous systems | |
CA2171129A1 (en) | Water treatment polymer containing poly¬oxy-¬(hydroxymethyl)-1,2-ethanediyl|| macromonomers and methods of use thereof | |
US5180790A (en) | Water soluble complexing agent for metallic cations | |
US7459513B2 (en) | Acrylic-acid-based homopolymers comprising taurine modified for the treatment of water | |
MX2014001453A (en) | Copolymers made of isoprenol, monoethylenically unsaturated monocarboxylic acids and sulphonic acids, process for producing same and use of same as deposit inhibitors in systems conveying water. | |
CA1339521C (en) | Composition and method for preventing corrosion in aqueous systems | |
CA1174451A (en) | Low level zinc corrosion inhibitors | |
EP0037221B1 (en) | Method and composition for inhibiting corrosion of metal surfaces in aqueous solutions |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PBP | Patent lapsed | ||
B1 | Patent granted (law 1993) | ||
PBP | Patent lapsed |